CN209829277U

CN209829277U - Flotation device and flotation system comprising a flotation device

Info

Publication number: CN209829277U
Application number: CN201920200671.0U
Authority: CN
Inventors: A·林内; P·伯克
Original assignee: Ottotai (finland) Co
Current assignee: Metso Minerals Ltd; Metso Finland Oy
Priority date: 2017-02-15
Filing date: 2019-02-14
Publication date: 2019-12-24
Anticipated expiration: 2029-02-14
Also published as: EP3582899A4; EP3582898A4; EP3582898A1; AU2017398923A1; CN110152892A; AU2021202827B2; WO2018150076A1; EA201991783A1; CA3053080A1; WO2018150094A1; ZA201905593B; AU2021202827A1; MX2022006696A; US11548013B2; EA201991776A1; EP3582897A4; US20190388905A1; MX2022006697A; CA3053078A1; CN110152891A

Abstract

The utility model relates to a flotation device and flotation system including the flotation device for handle the mineral ore granule of suspension in thick liquids. The flotation device comprises: a primary flotation circuit having a rougher section including at least two rougher primary flotation cells and a scavenger section including at least two scavenger primary flotation cells; and a secondary flotation circuit comprising at least two secondary flotation cells. The first secondary flotation cell is arranged to receive a primary overflow from the at least one rougher primary flotation cell and the other secondary flotation cell receives a primary overflow from at least one other rougher primary flotation cell. The further secondary flotation cell is arranged in fluid communication with a preceding secondary flotation cell and the underflow from the first secondary flotation cell is arranged to flow into the further secondary flotation cell or is arranged to be combined with the secondary underflow of the further secondary flotation cell.

Description

Flotation device and flotation system comprising a flotation device

Technical Field

The present disclosure relates to a flotation device and a flotation system comprising a flotation device for separating ore particles containing a valuable metal from ore particles suspended in a slurry.

Background

The overall efficiency of prior art flotation devices needs to be improved while the energy consumption or space required for the flotation device is large.

Prior art flotation devices require high energy consumption pumping, the overflow grade is to be improved, and the effective total recovery of ore particles containing valuable minerals is to be improved.

SUMMERY OF THE UTILITY MODEL

A flotation device is provided for processing mineral ore particles suspended in a slurry. The flotation apparatus includes a flotation tank for separating the slurry into an underflow and an overflow. The separation is carried out with the aid of a flotation gas. The flotation apparatus comprises a primary flotation circuit comprising a rougher section having at least two rougher primary flotation cells connected in series and arranged in fluid communication, the overflow from a first rougher primary flotation cell being arranged to flow directly into the secondary flotation circuit; the primary flotation circuit further comprises a scavenger section having at least two scavenger primary flotation cells connected in series and arranged in fluid communication, the overflow from the scavenger primary flotation cells being arranged to flow back into the rougher flotation cells of the primary flotation circuit or to a regrind step and then to the scavenger cleaner flotation circuit. In the first stage flotation circuit, a subsequent first stage flotation cell is arranged to receive a first stage underflow from a preceding first stage flotation cell. The secondary flotation circuit comprises at least two secondary flotation cells, wherein in the secondary flotation circuit the first secondary flotation cell is arranged in fluid communication with at least one rougher primary flotation cell and is arranged to receive a primary overflow from the at least one rougher primary flotation cell for recovering a first concentrate. The flotation apparatus is characterised in that in the secondary flotation circuit, a further secondary flotation cell is arranged in fluid communication with at least one further rougher primary flotation cell and arranged to receive a primary overflow from the at least one further rougher primary flotation cell to recover the first concentrate; the further secondary flotation cell is arranged in fluid communication with a preceding secondary flotation cell and the underflow from the first secondary flotation cell is arranged to flow into the further secondary flotation cell or is arranged to be combined with the secondary underflow of the further secondary flotation cell.

The use of the flotation device according to the invention is intended for the recovery of mineral ore particles containing valuable minerals.

The flotation system according to the invention comprises a flotation device according to the invention.

A flotation process for treating mineral ore particles suspended in a slurry in flotation stages, wherein the slurry is separated into an underflow and an overflow with the aid of a flotation gas, the flotation process comprising subjecting the slurry to a primary flotation comprising at least two rougher flotation stages connected in series and in fluid communication, the primary overflow from the first rougher flotation stage being directed to a secondary flotation; the first flotation stage further comprises at least two scavenger flotation stages in series and in fluid communication, the first overflow from the scavenger flotation stage being directed back to the first rougher stage or to regrind and then cleaner flotation, and in the first flotation stage the first underflow from the preceding flotation stage being directed to the subsequent flotation stage. In the flotation process, the slurry is further subjected to secondary flotation, which comprises at least two secondary flotation stages in fluid communication, wherein the primary overflow from at least the first rougher flotation stage is conducted to the first secondary flotation stage to recover the first concentrate, the at least the first rougher flotation stage and the first secondary flotation stage being connected in series and in fluid communication. The flotation process is characterized in that in a secondary flotation stage, primary overflow from at least one further rougher flotation stage is conducted to a further secondary flotation stage, which further secondary flotation stage is in series and in fluid communication with the at least one further rougher flotation stage for recovering the first concentrate, the at least one further rougher flotation stage and the further secondary flotation stage being in series and in fluid communication; the further secondary flotation stage and the preceding secondary flotation stage are in fluid communication; the underflow from the first secondary flotation stage is directed to or combined with the secondary underflow of the further secondary flotation stage.

With the invention described herein, the focus of slurry processing can be shifted to efficiently separate the non-value fraction from the ore particles and recover the maximum amount of value particles. In other words, ore particles containing very small amounts or even minimum amounts of valuable materials can be recovered for further processing. This is particularly advantageous for poor grade ores, i.e. ores that initially have very little valuable material, for example from lean deposits that have previously been considered economically too insignificant to be utilized.

Basically, ore particles containing a relatively large amount of valuable minerals are processed only once in a primary flotation circuit, which may be understood as a processing circuit comprising a rougher and/or scavenger cell. The underflow from the primary flotation tank is directed downstream along the primary flotation circuit to ensure that as much valuable mineral material as possible is recovered in the primary flotation circuit. At the same time, the overflow from the primary flotation cell is led to a secondary flotation circuit, which may be understood as a treatment circuit comprising a concentration cell for effectively separating any undesired particles from the material recovered in the primary circuit flotation cell. By directing the secondary underflow from the first secondary flotation tank downstream along the secondary flotation line, it is further ensured that as much valuable mineral material as possible is recovered.

Furthermore, when the underflow or overflow from the primary or secondary flotation cell is directed downstream by gravity in the direction of the flow of the slurry along the primary or secondary flotation circuit into the secondary flotation circuit, the energy consumption can be suppressed while still recovering the valuable minerals very efficiently.

High grade can be achieved for a part of the pulp flow while high recovery is achieved for the whole pulp flow through the flotation unit. Reprocessing the slurry stream in a plurality of adjacent flotation cells in this manner ensures efficient recovery of minerals without significantly increasing energy consumption, as the slurry flow does not need to be pumped in an energy consuming manner, but rather takes advantage of the inherent hydraulic pressure differential of the slurry stream downstream within the flotation apparatus and system.

Thus, high grade ore particles containing valuable minerals can be recovered at the beginning or front end of the flotation device, while at the end of the flotation device it can be used to recover as much ore particles containing even small amounts of valuable minerals as possible. By using a secondary flotation circuit, the grade of the overflow is increased, while in particular the primary flotation circuit ensures an efficient total recovery of ore particles containing valuable minerals. Flotation devices are able to upgrade without high energy consuming pumping and therefore offer significant advantages over the prior art.

The flotation device, the application thereof, the flotation system and the flotation method have the technical effects that: various particle sizes can be flexibly recovered, and ore particles containing valuable minerals can be efficiently recovered from lean ore feedstocks that initially contain smaller amounts of valuable minerals. The flotation circuit structure provides the advantages that: allowing for precise adjustment of flotation circuit structural parameters at various installation sites based on the target valuable material.

By treating the slurry according to the invention defined by the present disclosure, the recovery of particles containing valuable material can be increased. The initial grade of the recovered material is low, but the material (i.e. the slurry) is therefore also readily ready for further processing, which may include, for example, regrinding and/or beneficiation.

Arranging the flotation circuit so that at least some or all of the flotation cells, i.e. the flotation cell bottoms, are on the same level increases the construction speed, simplifies planning and construction and thus reduces costs. The so-called coplanarity of such flotation cells or flotation circuits may provide advantages by reducing investment costs, since less ground work and less space is required for establishing the system. This is particularly advantageous when the size of the flotation cell is increased. This is desirable from the standpoint of optimizing process performance while reducing capital investment costs. In case the flotation cells are arranged in a coplanar manner, the flow of slurry from one flotation cell to the next can be achieved by a pumping action, e.g. by a low-lift pump.

According to some embodiments of the invention, the flotation circuit may also be arranged in a step-wise manner, so that at least some of the flotation cells (i.e. the flotation cell bottoms) in the primary flotation circuit or in the secondary flotation circuit are located at different levels: for example, the bottom of a first primary flotation cell of a primary flotation circuit may be arranged higher than the bottom of a subsequent further primary flotation cell (rougher or cleaner primary), and/or higher than the bottom of a first secondary flotation cell to which the overflow of the first primary flotation cell is directed. In this way, the slurry surface level of at least some of the flotation cells after the first primary flotation cell is low, so that a step is formed between any two successive flotation cells that are in direct fluid connection with each other. The resulting step allows to achieve a hydrostatic head or a hydrostatic difference (hydraulic gradient) between two successive flotation cells, so that the flow of slurry from one cell to the next can be achieved by gravity without any separate pump. The hydraulic gradient forces the flow of slurry towards the tailings outlet of the flotation circuit. This may reduce the need for additional pumping. Furthermore, the pumping power requirement may be reduced, since the material flow is directed downstream by gravity due to the slurry surface height difference. This may even be applied to embodiments where the pulp surface level of adjacent flotation cells in the flotation circuit is at a level. The reduced need for energy intensive pumping will result in energy savings and a simplified construction of the flotation operation and a reduced need for construction space.

The at least one first primary overflow is directed to at least one stage of the first secondary flotation to recover the first concentrate, which means that the process does not comprise a grinding step between the primary flotation stage and the secondary flotation stage. By eliminating this grinding step, the hydraulic head of the slurry stream is not lost between any two successive stages, and gravity alone can be used to drive the slurry flow. Thus, the first stage overflow can be separated from the other stage overflows of lower grade. The first overflow may be floated separately from the other first overflows, which increases the recovery of ore particles containing valuable minerals.

Basically, flotation aims at recovering a concentrate of ore particles containing valuable minerals. Concentrate herein refers to the portion of the slurry withdrawn from the flotation cell in the overflow or underflow stream. By value mineral is meant any mineral, metal or other material of commercial value.

Flotation involves phenomena related to the relative buoyancy of the objects. The term flotation includes all flotation techniques. Flotation may be, for example, froth flotation, Dissolved Air Flotation (DAF) or induced air flotation. Froth flotation is a process of separating hydrophobic materials from hydrophilic materials by adding a gas (e.g. air or nitrogen or any other suitable medium) to the process. Froth flotation can be performed based on natural hydrophilic/hydrophobic differences or based on hydrophilic/hydrophobic differences created by the addition of surfactants or collectors. The gas can be added to the flotation feed (slurry or pulp) in a number of different ways.

Flotation apparatus herein refers to an assembly comprising a plurality of (at least two) flotation cells or cells that are fluidly connected to each other to form a flotation circuit to allow gravity driven or pumped slurry to flow between the flotation cells. Flotation devices are used to treat mineral ore particles suspended in a slurry by flotation. Thus, ore particles containing valuable metals are recovered from ore particles suspended in the slurry. The slurry is fed through a feed inlet to a first flotation cell of the flotation circuit to initiate the flotation process. The flotation device may be part of a larger flotation system containing one or more flotation devices. Thus, as is known to those skilled in the art, a plurality of different pre-treatment devices or stages and post-treatment devices or stages may be operatively connected to the components of the flotation device.

A flotation circuit is here a part of a flotation plant in which a plurality of flotation cells are arranged in fluid connection with each other so that the underflow of each preceding flotation cell is led as feed to the following flotation cell up to the last flotation cell of the flotation circuit, from which the underflow is led out of the flotation circuit as tailings or reject flow. With respect to the flotation process according to the invention, flotation here refers to the whole flotation process carried out in the flotation circuit.

The flotation cells in the flotation device are in fluid connection with each other. The fluid connection may be achieved by conduits of different lengths (e.g. pipes or tubes), the length of the conduits depending on the overall physical structure of the flotation device.

Alternatively, the flotation cells may be arranged in direct cell connection with each other. Direct cell connection here refers to an arrangement in which the outer walls of any two successive flotation cells are connected to each other to allow the outlet of a first flotation cell to be connected to the inlet of a subsequent flotation cell without any separate conduit. Direct contact reduces the need for piping between two adjacent flotation cells. Thus, the need for components during construction of the flotation circuit is reduced, thereby speeding up the construction process. In addition, the sand work can be reduced, and the maintenance of the flotation circuit is simplified.

The fluid connection between the flotation cell and the flotation unit may be direct, i.e. two flotation cells (belonging to the same or different flotation circuits) may be in close proximity to each other. Alternatively, the two flotation cells may be located at a distance from each other and connected by pipes, channels or other means known in the art. The fluid connection between the flotation cells may include various throttling mechanisms.

By "adjacent" flotation cells is meant here the flotation cell immediately after or before any one flotation cell, downstream or upstream, in the primary circuit or the secondary circuit, or the relationship between the flotation cell of the primary circuit and the flotation cell of the secondary circuit to which the overflow from the flotation cell of the primary circuit is directed.

A flotation cell is herein referred to as a tank or container in which a flotation process step is carried out. The flotation cell is generally cylindrical and is defined in shape by an outer wall. Flotation cells generally have a circular cross section. The flotation cell may also have a polygonal (e.g. rectangular, square, triangular, hexagonal or pentagonal) or other radially symmetrical cross-section. As known to those skilled in the art, the number of flotation cells may vary depending on the particular flotation device and/or operation used to process a particular type and/or grade of ore. With respect to the flotation process according to the invention, the flotation stage herein refers to a flotation process carried out in one flotation cell.

The flotation cell may be a froth flotation cell, such as a mechanically agitated cell or tank cell, a column flotation cell, a Jameson cell or a double flotation cell. In a double flotation cell, the cell comprises at least two separate vessels, the first mechanically agitated pressure vessel having a mixer and flotation gas inlet, the second vessel having a tailings outlet and an overflow froth outletThe vessels are arranged to receive the agitated slurry from the first vessel. The flotation cell may also be a fluid bed flotation cell (e.g. HydroFloat)^TMA tank) in which air or other flotation bubbles distributed by the fluidization system permeate through the hindered settling zone and attach to the hydrophobic component, thereby changing its density and floating it sufficiently for recovery. In a fluidized bed flotation cell, no axial mixing is required. The flotation cell may also be of a type in which a mechanical flotation cell (i.e. a flotation cell comprising a mechanical stirrer or mixer) comprises a microbubble generator for generating microbubbles in the slurry in the flotation cell. The size distribution of the microbubbles is smaller than that of conventional flotation bubbles introduced by a mixer or other gas introduction system (typically in the size range of 0.8-2 mm). The size of the microbubbles may range from 1 μm to 1.2 mm. The microbubbles may be introduced through a microbubble generator or a direct bubbling system including a slurry recirculation system.

The flotation cell may also be an overflow flotation cell operating with constant slurry overflow. In an overflow flotation cell, the slurry is treated by introducing flotation bubbles into the slurry and by creating a continuous upward flow of slurry in the vertical direction of the first flotation cell. At least a portion of the ore particles containing the metal are attached to the bubbles and rise upwardly by buoyancy, at least a portion of the ore particles containing the value metal are attached to the bubbles and rise upwardly as the slurry continues to flow upwardly, and at least a portion of the ore particles containing the value metal rise upwardly as the slurry continues to flow upwardly. Ore particles comprising valuable metals are recovered by directing a continuous upward flow of slurry as a slurry overflow out of the at least one overflow flotation tank. Since the overflow launder operates with little froth depth or froth layer, there is little froth zone formed on the surface of the pulp at the top of the flotation cell. The foam may be discontinuous over the channels. As a result, more ore particles containing valuable minerals can be entrained into the concentrate stream and the overall recovery of valuable material can be increased.

All flotation cells of the flotation apparatus according to the invention may be of a single type, i.e. the rougher flotation cell in the rougher section, the scavenger flotation cell in the scavenger section, and the secondary flotation cell of the secondary flotation circuit may be of a single cell type, so that the flotation apparatus comprises only one flotation cell as listed above. Alternatively, the plurality of flotation cells may be of one type and the other cells of one or more types, whereby the flotation apparatus comprises more than two flotation cells as listed above.

Depending on its type, the flotation cell may include a mixer for agitating the slurry to keep it in suspension. By mixer is meant herein any suitable device for agitating the slurry in the flotation cell. The mixer may be a mechanical stirrer. The mechanical agitator may comprise a rotor-stator structure with a motor and a drive shaft, the rotor-stator structure being arranged at the bottom of the flotation tank. The flotation cell may have an auxiliary agitator arranged higher up in the vertical direction of the flotation cell to ensure a sufficiently strong and continuous upward flow of the slurry.

Overflow in this context refers to the portion of the slurry that collects in the launder of the flotation cell and thus leaves the flotation cell. The overflow may include foam, foam and slurry, or in some cases only slurry or the largest portion is slurry. In some embodiments, the overflow may be an accept stream containing particles of valuable material collected from the slurry. In other embodiments, the overflow may be a waste stream. This is the case when the flotation device, system and/or method is used for reverse flotation.

Underflow in this context refers to the portion of the slurry that does not float to the surface of the slurry during flotation. In some embodiments, the underflow may be a reject stream that exits the flotation cell through an outlet that is typically disposed in a lower portion of the flotation cell. Finally, the underflow from the final flotation cell of the flotation circuit or flotation unit can leave the whole unit as a tailings stream or the final residue of the flotation system. In some embodiments, the underflow may be an accept stream containing valuable mineral particles. This is the case when the flotation device, system and/or method is used for reverse flotation.

Reverse flotation in this context refers to the reverse flotation process commonly used for iron recovery. In this case, the flotation process is used to collect the non-valuable part of the slurry flow into the overflow. The overflow of iron in the reverse flotation process usually contains silicates, while the mineral particles containing valuable iron are collected in the underflow. Reverse flotation can also be used for industrial minerals, i.e. to develop geological minerals of commercial value that are neither fuels nor metal sources, such as bentonite, silica, gypsum and talc.

Downstream in this context refers to the direction co-current with the slurry flow (forward flow, indicated by arrows in the figure), and upstream in this context refers to the direction counter-current or against the slurry flow.

Concentrate in this context means the floating part of the slurry containing ore particles of valuable minerals. The first concentrate may comprise ore particles containing one mineral value and the second concentrate may comprise ore particles containing another mineral value. Alternatively, the first and second distinguishing terms may refer to two ore particle concentrates comprising the same value mineral but having two distinct particle size distributions.

Rougher flotation, the rougher section of the flotation circuit, the rougher stage and/or the rougher tank refer herein to the flotation stage that produces a rougher concentrate. The aim is to remove the maximum amount of valuable minerals with the greatest possible coarse grain size. Rougher flotation does not require complete dissociation, and the degree of dissociation need only be sufficient to liberate enough gangue from the valuable minerals for high recovery. The main objective of the roughing stage is to recover as much valuable minerals as possible, but less attention is paid to the quality of the produced concentrate.

The rougher concentrate is usually subjected to a concentration flotation stage in a rougher concentration flotation circuit in order to reject more of the unwanted minerals that have reached the froth in a process called concentration. The concentration product is called concentrate or final concentrate.

Rougher flotation is usually followed by scavenger flotation for rougher tailings. Scavenger flotation, the scavenger section of the flotation circuit, the scavenger stage and/or the scavenger cell refer to a flotation stage intended to recover any valuable mineral material that was not recovered during the initial rougher stage. This can be achieved by varying the flotation conditions to be more stringent than the initial rougher flotation, or in some embodiments of the invention by introducing microbubbles into the slurry. Concentrate from the scavenger cell or scavenger stage can be returned to the rougher feed for refloating or directed to a regrinding step and then to a scavenger concentration flotation circuit.

Concentration flotation, rougher/scavenger concentration line, concentration stage and/or concentration tank refer to a flotation stage, the purpose of which is to produce as high a concentrate grade as possible.

Pretreatment and/or aftertreatment and/or further processing refer, for example, to comminution, grinding, separation, screening, fractionation, conditioning or beneficiation, all of which are conventional methods known to those skilled in the art. The further processing may further comprise at least one of: another secondary flotation cell, which may be a conventional concentration flotation cell, a recovery cell, a rougher cell or a scavenger cell.

The pulp surface height in this context refers to the pulp surface height in the flotation cell measured from the bottom of the flotation cell to the launder lip of the flotation cell. In practice, the pulp height is equal to the height of the launder lip of the flotation cell, measured from the bottom of the flotation cell to the launder lip of the flotation cell. For example, any two successive flotation cells may be arranged in a flotation circuit in a stepwise manner such that the pulp surface heights of the flotation cells are different (i.e. the pulp surface height of the first flotation cell is higher than the pulp surface height of the second flotation cell). This difference in the level of the slurry surface is defined herein as the "step" between any two successive flotation cells. A step or difference in the height of the surface of the slurry is a difference that allows gravity-driven slurry flow by creating a hydraulic head between two successive flotation cells.

In one embodiment of the flotation apparatus, the at least one secondary flotation cell of the secondary flotation circuit is arranged in direct fluid communication with a first rougher primary flotation cell from which the primary overflow is received.

Direct fluid communication in this context means that any two adjacent flotation cells are connected such that there are no additional process steps, such as grinding, arranged between any two flotation cells or flotation stages. This should not be confused with the definition of a direct slot connection as described above.

In some cases of conventional froth flotation processes, the overflow of the first flotation cell may be directed first to a regrinding step or to other further processing steps before being introduced into the secondary flotation cell. This is particularly typical for conventional flotation operations that include a rougher or scavenger stage followed by a cleaner stage.

In the flotation device, system and method according to the invention, such further processing steps can be dispensed with and the rougher primary flotation cell and the secondary flotation cell into which the primary overflow of the rougher primary flotation cell is introduced are directly fluidically connected to one another. A similar direct fluid communication may also be arranged between any other two flotation cells of the flotation apparatus.

In one embodiment of the flotation apparatus, the primary flotation circuit comprises at least four primary flotation cells, or 3-10 flotation cells, or 4-7 flotation cells.

In one embodiment of the flotation apparatus, the rougher section of the primary flotation circuit comprises at least two rougher primary flotation cells, or 2-6 rougher primary flotation cells, or 2-4 primary flotation cells.

In one embodiment of the flotation apparatus, the scavenger section of the primary flotation circuit comprises at least two scavenger primary flotation cells, or 2-6 scavenger primary flotation cells, or 2-4 scavenger primary flotation cells.

A sufficient number of primary flotation cells (rougher and/or scavenger primary flotation cells) can produce part of the high grade concentrate while ensuring a high recovery of the desired value minerals in the whole primary circuit, thereby avoiding leaving any value minerals in the tailings stream. As much ore particles containing valuable minerals as possible float while still minimizing the pumping energy required to achieve this.

In one embodiment of the flotation apparatus, the secondary circuit comprises at least two secondary flotation cells, or 2-10 secondary flotation cells, or 4-7 secondary flotation cells.

Even a small number of secondary flotation cells is sufficient to concentrate the overflow of the primary flotation cell to a reasonable level, i.e. to upgrade the concentrate recovered from the primary circuit. Even the flow of underflow from a small number of secondary flotation cells is sufficient to be sent to the primary flotation circuit for further processing to further increase recovery.

In one embodiment of the flotation apparatus, the number of secondary flotation cells in series in the secondary flotation circuit is the same or less than the number of primary flotation cells in series in the primary flotation circuit.

The quality (i.e. grade) of the overflow from the primary flotation cell to the first flotation cell of the secondary flotation circuit may be higher than the overflow from the primary flotation cell located further downstream in the primary flotation circuit to the further secondary flotation cell of the secondary flotation circuit. Thus, additional secondary flotation cells of the secondary flotation circuit may require greater capacity to effectively treat the slurry. Furthermore, the over-treatment in the first secondary flotation cell leads to increased pumping requirements, which leads to an undesirably increased energy consumption. The effect of this embodiment is: at least a portion of the concentrate can be recovered at a very high grade while minimizing the driving of the slurry stream by pumping.

In one embodiment of the flotation apparatus, the secondary flotation cell is arranged to receive a primary overflow from 1-3 rougher primary flotation cells or 1-2 rougher primary flotation cells.

In another embodiment of the flotation apparatus, the secondary flotation cell is arranged to receive a primary overflow from at most two rougher primary flotation cells.

In another embodiment of the flotation apparatus, the secondary flotation cell is arranged to receive a primary overflow from at most one rougher primary flotation cell.

In a further embodiment of the flotation apparatus, the further secondary flotation cell is arranged to receive a primary overflow from at least two rougher primary flotation cells.

In this way the overflows of the different rougher primary flotation cells do not mix to a very high degree. Each overflow can then be treated in the best possible way to ensure adequate treatment and only a small number of secondary flotation cells acting as recovery cells are needed to obtain a high grade concentrate.

In one embodiment of the flotation apparatus, the underflow from the further secondary flotation cell is arranged to flow back to the rougher section of the primary flotation circuit at a point downstream of the rougher primary flotation cell from which the further secondary flotation cell receives the primary overflow.

In another embodiment of the flotation apparatus, the underflow from the further secondary flotation cell is arranged to flow back into the further rougher primary flotation cell downstream of the first rougher primary flotation cell from which the further secondary flotation cell receives the primary overflow.

In a further embodiment the underflow from the further secondary flotation cell is arranged to be combined with the overflow of at least one further rougher primary flotation cell downstream of the rougher primary flotation cell from which the further secondary flotation cell receives the primary overflow.

In one embodiment of the flotation apparatus, the secondary flotation circuit further comprises an additional secondary flotation circuit comprising at least one additional secondary flotation cell arranged to receive a primary overflow from at least one other rougher primary flotation cell.

In another embodiment of the flotation apparatus, the underflow from the further secondary flotation cell is arranged to flow into an additional secondary flotation cell.

In another embodiment of the flotation apparatus, the first secondary flotation cell is arranged to receive a primary overflow from the first rougher primary flotation cell, and the additional secondary flotation cell is arranged to receive a primary overflow from at least two further rougher primary flotation cells.

An additional secondary flotation cell can be used as a recovery cell. In fact, this arrangement can prevent ore particles containing valuable minerals from ending up in the tailings stream, thereby further ensuring good recovery of the desired concentrate.

By using an additional secondary flotation cell it can be ensured that all available valuable minerals flow from the slurry stream of the primary flotation circuit back into the revenue overflow or concentrate. The loss of ore particles containing valuable minerals can be minimized further improving the froth recovery efficiency of the flotation apparatus and system. Similarly, when using a flotation unit in reverse flotation, as many ore particles containing valuable material as possible can be recovered in the underflow from the primary flotation circuit. The underflow from the additional secondary flotation tank may be directed to a regrinding circuit or step to ensure recovery of ore particles containing valuable minerals from the slurry stream.

Furthermore, the need for pumping can be reduced while the underflow of the secondary flotation circuit is effectively reprocessed. The use of an additional secondary flotation cell as a recovery cell after this operation allows for efficient flotation of a large portion of the ore particles containing valuable minerals. From the primary circuit, where high grade concentrate has been taken, a sufficient amount of primary overflow can still be collected to effectively float away the desired concentrate. In addition, the underflow from the additional secondary flotation tank can be directed to further processing steps. This underflow stream may be particularly suitable for further grinding steps.

An additional secondary flotation cell in this context means a flotation cell from which the overflow is led out of the flotation device, for example directly into a further processing step, for example a grinding step or a frothing step. The underflow of the additional secondary flotation cell may be directed back to the first rougher primary flotation cell upstream into the primary flotation circuit, or to a rougher primary flotation cell upstream of the rougher primary flotation cell from which the additional secondary flotation cell receives overflow, or directed out of the flotation unit, either as a tailings stream to further processing external to the flotation unit, such as regrinding, or as feed to another flotation unit to recover another concentrate.

In one embodiment of the flotation apparatus, the underflow from the further secondary flotation cell is arranged to flow into the last rougher primary flotation cell of the at least one rougher primary flotation cell from which the further secondary flotation cell receives a primary overflow, or into the rougher primary flotation cell downstream of the last rougher primary flotation cell of the at least one rougher primary flotation cell from which the further secondary flotation cell receives a primary overflow.

When the underflow from the secondary flotation tank is returned downstream in the flow direction of the slurry to the primary flotation circuit, energy consumption can be suppressed while still achieving a very efficient recovery of valuable minerals. High grade can be obtained for a part of the pulp flow, while a high recovery is obtained for the whole pulp flow through the flotation unit. Directing the underflow downstream from the secondary flotation tank avoids energy intensive pumping. Reprocessing the slurry stream in a plurality of adjacent flotation cells in this manner ensures efficient recovery of minerals without any significant increase in energy consumption, as the flow of slurry does not need to be pumped in an energy consuming manner, but rather takes advantage of the inherent hydraulic head of the downstream slurry stream within the flotation apparatus and system. The slurry is returned to the flotation device to a location where similar slurry has been processed for further processing. In fact, any pumping required to drive the slurry flow can be minimized while the slurry is still directed to multiple processing stages in the flotation device. Furthermore, slurry portions having similar or identical properties may be combined for further processing. The primary flotation circuit underflow and the secondary circuit underflow combination may have very similar properties, such as the amount of ore particles still containing valuable minerals, or ore particles having the same particle size distribution. Thus, the operation of the flotation process can be optimized.

In one embodiment of the flotation device, the first secondary flotation cell of the secondary flotation circuit has a larger volume than the further secondary flotation cell of the secondary flotation circuit.

The concentrate grade in the overflow of the first primary flotation cell may be higher than in the later primary flotation cell in the primary flotation circuit. The overflow from those later stage flotation cells can then be treated in a smaller secondary flotation cell, resulting in a shorter flotation time. This arrangement ensures that the concentrate from the further secondary flotation cell of the secondary flotation circuit is of higher grade.

In one embodiment of the flotation device, the volume of the further secondary flotation cell of the secondary flotation circuit is larger than the volume of the first secondary flotation cell of the secondary flotation circuit.

In one embodiment of the flotation plant, the first rougher primary flotation cell has a volume of at least 150m³Or a volume of at least 500m³Or at least 2000m³。

In one embodiment of the flotation plant, the second rougher primary flotation cell has a volume of at least 100m³Or a volume of at least 300m³Or at least 500m³。

The use of a flotation cell having a volume of at least 400 cubic metres increases the likelihood of air bubbles generated in the flotation cell (e.g. by the rotor) colliding with particles containing the valuable mineral, thereby increasing the recovery of the valuable mineral and the overall efficiency of the flotation apparatus. Larger flotation cells have higher selectivity because the longer the slurry stays in the cell, the more collisions between the bubbles and the ore particles. Thus, most of the ore particles containing valuable minerals can float. Furthermore, the fall back of the floating ore particles will be greater, which means that ore particles containing a very small amount of valuable minerals fall back to the bottom of the flotation tank. Thus, the overflow from the larger flotation cell and/or the grade of the concentrate will be higher. The primary flotation tank for roughing can ensure high grade.

In one embodiment of the flotation apparatus, the volume of the second rougher primary flotation cell is the same as or smaller than the volume of the first rougher primary flotation cell.

In one embodiment of the flotation apparatus, the first secondary flotation cell in fluid communication with the rougher primary flotation cell has a volume of 100-³The preferred volume is 400-³。

The use of a flotation cell having a volume of at least 400 cubic metres increases the likelihood of air bubbles generated in the flotation cell (e.g. by the rotor) colliding with particles containing the valuable mineral, thereby increasing the recovery of the valuable mineral and the overall efficiency of the flotation apparatus. As mentioned above, larger flotation cells have higher selectivity because the longer the slurry stays in the flotation cell, the more collisions between bubbles and ore particles. Thus, most of the ore particles containing valuable minerals can float. Furthermore, the fall back of the floating ore particles will be greater, which means that ore particles containing a very small amount of valuable minerals fall back to the bottom of the flotation tank. Thus, the overflow of the larger flotation cell and/or the grade of the concentrate is higher.

In one embodiment of the flotation device, the volume of the further secondary flotation cell of the secondary flotation circuit in fluid communication with the rougher primary flotation cell is 100-³Preferably 300-1000m³。

The use of a flotation cell having a volume of at least 300 cubic metres increases the likelihood of collisions between gas bubbles generated in the flotation cell (e.g. by the rotor) and particles containing valuable minerals, thereby improving the recovery of valuable minerals and the overall efficiency of the flotation apparatus.

In one arrangement, a secondary flotation circuit concentrates the overflow from the rougher primary flotation cell and the underflow from the secondary flotation circuit is directed back to the rougher primary flotation cell further downstream, where higher grade is more important than obtaining a high recovery of ore particles containing valuable minerals in the overflow of the rougher primary flotation cell. This is because the underflow from the secondary flotation circuit can be reprocessed in the primary flotation circuit and any remaining ore particles containing valuable minerals are then recovered. Although some valuable material is directed back into the primary flotation circuit, the energy required to pump the underflow back into the primary flotation circuit is not important, since the later rougher primary flotation cell ensures recovery. Thus, volumes of up to 2000m can be used³Very large flotation cells. However, use is made of more than 1000m³The flotation cell of (a) is not always preferred because efficient mixing is difficult in such large cells. Without effective mixing, ore particles containing relatively small amounts of valuable minerals fall back to the bottom of the flotation cell, which negatively affects recovery.

With the flotation device of the above embodiment, at least a part of the concentrate can be produced or recovered at a very high grade.

If the first rougher primary flotation cell has a relatively large volume, then a large subsequent flotation cell may not be required, and thus the flotation cell (primary or secondary) downstream of the first rougher primary cell may be smaller and therefore more efficient. In the flotation of certain minerals, it is easy to float a large part of the ore particles containing valuable minerals at high grade. In this case there may be a smaller volume of flotation cells downstream of the primary flotation circuit and still a high recovery rate can be achieved.

In one embodiment of the flotation apparatus, the volume of the first secondary flotation cell in fluid communication with the at least one rougher primary flotation cell is 2-50% of the total volume of the at least one rougher primary flotation cell, preferably 3-30% of the total volume of the at least one rougher primary flotation cell.

In one embodiment of the flotation apparatus, the volume of the further secondary flotation cell of the secondary circuit in fluid communication with the at least one rougher primary flotation cell is 2-50% of the total volume of the at least one rougher primary flotation cell, preferably 3-30% of the total volume of the at least one rougher primary flotation cell.

The total volume here refers to the combined volume of the rougher primary flotation cells from which the secondary flotation cell receives the primary overflow. For example, the further secondary flotation cell may receive a primary overflow from more than one rougher primary flotation cell of the primary flotation circuit. In this case, the total volume is the total volume of each rougher primary flotation cell.

In such an embodiment, a portion of the concentrate is produced at high grade. When the secondary flotation cell of the secondary flotation circuit is small, the residence time of the ore particles in the flotation cell, i.e. the time for flotation of the desired concentrate, is short. The concentrate thus obtained is therefore of higher grade.

Constructing the secondary flotation cell of the secondary flotation circuit smaller than the flotation cell in the primary flotation circuit in the direction of slurry flow can provide efficiency benefits. The effect is particularly pronounced if the flotation cell in the secondary flotation circuit is at least 10% smaller than the flotation cell in the primary flotation circuit. For example, the at least one flotation cell of the secondary flotation circuit may be at least 20 or 30% smaller than the at least one primary flotation cell of the primary flotation circuit.

In one embodiment of the flotation apparatus, the flow of slurry between the fluidly connected at least two flotation cells is driven by gravity.

In another embodiment of the flotation apparatus, the flow of slurry between the first rougher primary flotation cell and the further rougher primary flotation cell is driven by gravity.

In another embodiment of the flotation apparatus, the flow of slurry between the first secondary flotation cell and the further secondary flotation cell is driven by gravity.

In another embodiment of the flotation apparatus, the flow of slurry between the rougher primary flotation cell and the secondary flotation cell in fluid connection with the rougher primary flotation cell is driven by gravity.

In another embodiment of the flotation apparatus, the flow of slurry between the first rougher primary flotation cell and the first secondary flotation cell is driven by gravity.

In another embodiment of the flotation apparatus, the flow of slurry between the other rougher primary flotation cell and the other secondary flotation cell is driven by gravity.

By arranging for gravity driven slurry flow, savings in energy consumption can be achieved as no additional pumping is required to drive the slurry downstream.

By avoiding energy intensive pumping in the flotation unit, significant energy savings can be achieved while ensuring efficient recovery of valuable mineral material from poor grade ore (i.e. initially comprising even very few valuable minerals). A part of the concentrate of high grade can be produced, while a good overall recovery of the desired valuable minerals can be obtained. Only traces of valuable minerals are ultimately contained in the tailings stream.

The present invention aims to improve the mineral recovery process while reducing the energy consumption of the process. This can be achieved by utilizing the inherent slurry flow of the process, i.e. by moving the slurry flow to a reprocessing in a downstream flotation cell. By so arranging the flotation process, the flow of slurry can be directed by gravity. In some embodiments, the slurry flow may also be directed by low intensity pumping, or by a suitable combination of both, gravity and low intensity pumping. For example, the slurry may be flowed by a low-lift pump or gravity when the underflow from another secondary flotation cell is arranged to flow into the last rougher primary flotation cell in the at least one rougher primary flotation cell from which the another secondary flotation cell receives a primary overflow or into a rougher primary flotation cell downstream of the last rougher primary flotation cell in the at least one rougher primary flotation cell from which the another secondary flotation cell receives a primary overflow.

A low-head pump is herein understood to mean any type of pump that generates a low pressure to drive the slurry stream downstream. Typically, low-lift pumps produce a maximum lift of up to 1.0 meter, i.e. can be used to drive the flow of slurry between two adjacent flotation cells having a difference in the height of the slurry surface of less than 30 cm. Low-lift pumps may typically have an impeller for generating axial flow.

In one embodiment of the flotation apparatus, the primary overflow from at least one scavenger primary flotation cell is arranged to flow directly into the regrinding step.

In another embodiment of the flotation apparatus, the combined primary overflow from each scavenger primary flotation cell is arranged to flow directly into the regrinding step.

In one embodiment of the flotation apparatus, the combined secondary overflow of the at least two secondary flotation cells is arranged to flow into a further processing step.

In one embodiment of the flotation apparatus, the underflow from the last scavenger primary flotation cell is arranged to flow to further processing steps or to leave the flotation apparatus as tailings.

In one embodiment of the flotation apparatus, the underflow from the last secondary flotation cell of the secondary flotation circuit is arranged to flow to further processing steps or to leave the flotation apparatus as tailings.

In another embodiment of the flotation apparatus, the further processing step comprises at least one step selected from the group consisting of: grinding, adjusting and floating.

Further processing in this context refers to any suitable process step, such as a grinding step or a chemical addition step, or any other process step typically used in conjunction with a flotation device, as is known to those skilled in the art. The grinding step may comprise at least one grinder, which may be any suitable grinder known to those skilled in the art.

In one embodiment of the flotation apparatus, the flotation apparatus comprises two primary flotation circuits, and the first secondary flotation tank of the secondary flotation circuit is arranged to receive overflow from the first rougher primary flotation tank of the two primary flotation circuits.

In such an arrangement, a greater amount of slurry can be made to flow into the secondary flotation circuit. Thus, larger volume flotation cells can also be used in the secondary circuit, with benefits primarily related to efficiency, as discussed previously in this disclosure.

In one embodiment of the flotation apparatus, the primary flotation cell and/or the secondary flotation cell comprises a froth flotation cell.

In one embodiment of the flotation apparatus, the third rougher primary flotation cell and any subsequent rougher primary flotation cells after the third rougher primary flotation cell comprise froth flotation cells.

In another embodiment of the flotation apparatus, the first rougher primary flotation cell and the second rougher primary flotation cell of the primary flotation circuit operate as overflow flotation cells.

In another embodiment of the flotation apparatus, the flotation gas is fed into a flotation tank that separates the slurry into an overflow and an underflow.

In another embodiment of the flotation apparatus, the flotation cell into which the flotation gas is fed comprises a mixer.

In another embodiment of the flotation device, the flotation gas is fed to a prefloating cell in which a mixer is arranged.

A prefloat cell refers herein to a flotation vessel in which the slurry can be prepared for flotation, usually by introducing flotation gas and by using mechanical agitation, before it is introduced into a second vessel where the actual flotation process takes place. The preliminary flotation tank may for example be the first container of the dual flotation tank described previously in this disclosure.

In one embodiment of the flotation device, the mineral ore particles comprise Cu, or Zn, or Fe, or pyrite, or metal sulfides (e.g. gold sulfides). Mineral ore particles containing other valuable minerals, such as Pb, Pt, PGMs (platinum group metals Ru, Rh, Pd, Os, Ir, Pt), oxide minerals, industrial minerals (e.g., Li (i.e., spodumene), petalite), and rare earth minerals, may also be recovered according to various aspects of the invention.

One embodiment of the use of the flotation device according to the invention is particularly used for recovering mineral ore particles containing valuable minerals from low grade ore.

One embodiment of the use of the flotation device according to the invention is intended for recovering mineral ore particles containing Cu from low grade ore.

An embodiment of the use of the flotation device according to the invention is in a flotation device, wherein the first rougher primary flotation cell has a volume of at least 150m³Or a volume of at least 500m³Or at least 2000m³And wherein the flow of the slurry is driven by gravity.

An example of the use of the flotation device according to the invention is in a flotation device in which the volume of the second rougher primary flotation cell is at least 100m³Or a volume of at least 300m³Or at least 500m³And wherein the flow of the slurry is driven by gravity.

One embodiment of the use of a flotation device according to the invention is intended for a flotation device in which the flow of slurry between the primary flotation cells of a primary flotation circuit is driven by gravity.

One embodiment of the use of the flotation device according to the invention is intended for a flotation device in which the flow of slurry between the secondary flotation cells of the secondary circuit is driven by gravity.

One embodiment of the use of a flotation device according to the invention is intended for a flotation device, wherein the flow of slurry between a rougher primary flotation cell and a secondary flotation cell in fluid connection with the rougher primary flotation cell is driven by gravity.

One embodiment of the use of the flotation device according to the invention is intended for a flotation device, wherein the flow of slurry between the first rougher primary flotation cell and the first secondary flotation cell is driven by gravity.

One embodiment of the use of the flotation device according to the invention is intended for a flotation device in which the flow of slurry between another rougher primary flotation cell and another secondary flotation cell of a secondary flotation circuit is driven by gravity.

One embodiment of the use of the flotation device according to the invention is intended to recover mineral ore particles containing Fe by reverse flotation.

In one embodiment of the flotation system, the system comprises at least two or at least three flotation devices according to the invention.

In one embodiment of the flotation system, the system comprises at least one first flotation device for recovering a first concentrate and at least one second flotation device for recovering a second concentrate.

In one embodiment of the flotation system, the primary flotation cell of the at least one first flotation device for recovering the first concentrate and the primary flotation cell of the at least one second flotation device for recovering the second concentrate are arranged in series.

In one embodiment of the flotation system, the system further comprises means for further processing the mineral ore particles suspended in the slurry such that the second concentrate is different from the first concentrate.

In one embodiment of the flotation system, the apparatus for further processing of mineral ore particles suspended in the slurry comprises a grinding step, arranged between the first flotation device and the second flotation device.

In this case, the second concentrate recovered from the second flotation device may have a similar mineral composition to the first concentrate recovered from the first flotation device, but the particle size distribution of the slurry introduced into the second flotation device after the grinding step may be different.

In one embodiment of the flotation system, the system for further processing of mineral ore particles suspended in a slurry comprises a device for adding a flotation chemical, arranged between the first flotation device and the second flotation device.

In this case, the second concentrate recovered from the second flotation device may have a different mineral composition than the first concentrate recovered from the first flotation device, the flotation chemicals used naturally being determined by the desired valuable minerals to be recovered by the second flotation device.

In one embodiment of the flotation system, the flotation device is arranged to recover mineral ore particles containing Cu and/or Zn and/or pyrite and/or to recover metals (e.g. gold) from sulphides.

In an embodiment of the flotation system, the flotation system is arranged to recover mineral ore particles containing Cu from the low grade ore.

For example, in the recovery of copper from low grade ore obtained from lean deposits of mineral ore, the amount of copper can be as low as 0.1% by weight of the feed (i.e. slurry fed to the flotation unit). The flotation device according to the invention is very practical for the recovery of copper, since copper is a so-called floatable mineral. In the dissociation of ore particles containing copper, a relatively high grade can be obtained from the first primary flotation cell without any additional pumping between the flotation cells.

By using the flotation device according to the invention, the recovery of such small amounts of valuable minerals (e.g. copper) can be efficiently increased and even lean deposits can be cost-effectively utilized. As known rich deposits have been increasingly used, it is also highly necessary to treat less favorable deposits, which have not been previously mined due to the lack of suitable techniques and methods to recover the very low amounts of valuable material in the ore.

In another embodiment of the flotation system, the flotation device is arranged to recover Fe by reverse flotation.

In reverse flotation, mineral ore particles containing undesirable material are removed from the slurry by adhering gas bubbles to the mineral ore particles containing undesirable material and removing them from the overflow of the flotation cell, while the ore particles containing valuable mineral material are recovered in the underflow, thus reversing the accept stream of conventional flotation as the overflow and the reject stream as the underflow. In general, in the reverse flotation of Fe, the large mass pull of the worthless material (most commonly silicates) can cause significant problems in controlling the flotation process. Inevitably, some of the mineral ore particles containing valuable Fe will end up in the overflow (especially the fine and light particles). By directing this overflow to the secondary flotation circuit for reprocessing, at least some of the Fe-containing mineral ore particles can be processed into the underflow of the secondary flotation circuit and thus recovered.

Similarly, by using reverse flotation in the same way as for Fe, the slurry treatment for recovering industrial minerals such as bentonite, silica, gypsum or talc can be improved. In the recovery of industrial minerals, the goal of flotation can be, for example, the removal of dark particles into overflow waste, and the recovery of white particles into underflow accepts. In this process, some lighter and finer white particles eventually enter the overflow. In accordance with the present disclosure, these particles can be efficiently recovered by the present invention.

In one embodiment of the flotation process according to the invention, the slurry is subjected to at least four primary flotation stages, or 3-10 primary flotation stages, or 4-7 primary flotation stages.

In one embodiment of the flotation process, the slurry is subjected to at least two secondary flotation stages, or 2-10 secondary flotation stages, or 4-7 secondary flotation stages.

In one embodiment of the flotation process, the primary overflow from 1-3 rougher flotation stages or 1-2 rougher flotation stages is conducted to the secondary flotation stage.

In one embodiment of the flotation process, the primary overflow from at least one further rougher flotation stage and the secondary underflow from said further secondary flotation stage are directed to an additional secondary flotation stage of the secondary flotation.

In another embodiment of the flotation process, the primary overflow from the first rougher flotation stage is conducted to a first secondary flotation stage, and the primary overflow from at least two further rougher flotation stages is conducted to an additional secondary flotation stage.

In one embodiment of the flotation process, the underflow from the secondary flotation stage is directed to primary flotation in the last rougher flotation stage of the at least one rougher flotation stage from which the primary overflow is received, or to primary flotation in a rougher flotation stage downstream of the last rougher flotation stage of the at least one rougher flotation stage from which the primary overflow is received.

In one embodiment of the flotation process froth flotation is used in at least one primary flotation stage and/or at least one secondary flotation stage.

In one embodiment of the flotation process, overflow flotation is employed in the first rougher flotation stage, or in the first rougher flotation stage and the second rougher flotation stage.

Drawings

The accompanying drawings, which are included to provide a further understanding of the disclosure and are incorporated in and constitute a part of this specification, illustrate embodiments of the disclosure and together with the description help to explain the principles of the disclosure. In the drawings:

FIG. 1a is a flow chart of one embodiment of the present invention.

FIG. 1b is a flow chart of one embodiment of the present invention.

FIG. 2 is a flow chart of one embodiment of the present invention.

FIG. 3 is a flow chart of one embodiment of the present invention.

Fig. 4a is a flow chart of a detail of the embodiment of fig. 1 a.

Fig. 4b is a simplified schematic perspective view of the embodiment of fig. 4 a.

Fig. 4c is a flow chart of an alternative detail of the embodiment in fig. 1 a.

Figure 5a is a flow diagram of another detail of the flotation device.

Fig. 5b is a simplified schematic perspective projection view of the embodiment of fig. 5 a.

Figure 5c is a simplified illustration showing the relative vertical placement of the flotation cells as viewed from the direction of the secondary flotation cell of figure 5 a.

Figure 6a is a flow chart of details of one embodiment of the present invention.

Fig. 6b is a simplified schematic perspective projection view of the embodiment of fig. 6 a.

Figure 6c is a simplified illustration showing the relative vertical placement of the flotation cells as viewed from the direction of the secondary flotation cell of figure 6 a.

FIG. 7 is a flow chart of details of one embodiment of the present invention.

FIG. 8 is a flow chart of details of one embodiment of the present invention.

FIG. 9 is a flow chart of details of one embodiment of the present invention.

FIG. 10 is a flow chart of details of one embodiment of the present invention.

FIG. 11 is a flow chart of details of one embodiment of the present invention.

FIG. 12 is a flow chart of details of one embodiment of the present invention.

FIG. 13 is a flow chart of details of one embodiment of the present invention.

FIG. 14 is a flow chart of details of one embodiment of the present invention.

Figure 15 is a flow diagram of an embodiment of a flotation system according to the invention.

Figure 16 is a simplified schematic perspective projection view of a flotation cell.

Detailed Description

Reference will now be made in detail to embodiments of the present disclosure, examples of which are illustrated in the accompanying drawings.

The following description discloses certain embodiments in detail to enable those skilled in the art to utilize the devices, systems, and methods based on the present disclosure. Not all of the steps of an embodiment will be discussed in detail as many steps will be apparent to those of skill in the art based on this disclosure.

For the sake of simplicity, the reference numerals will be kept unchanged in the following exemplary embodiments, with the components being repeated.

Fig. 1a-14 show the flotation device 1 or a detailed part A, B of the flotation device 1, and fig. 15 shows the flotation system 9 in a schematic way. The flotation cell is shown in detail in figure 16. The figures are not drawn to scale and the flotation cell, flotation device 1 and various components of the flotation system 9 have been omitted for clarity. In order to fit the figure on a single drawing page, some connections between the flotation cells, flotation lines or flotation devices are shown as graphical lines of not-to-scale length, rather than actual-size-to-scale connections. The forward direction of the flow of slurry is indicated by the arrows in the figure.

Although flotation is disclosed in the following examples mainly by reference to froth flotation, it should be noted that the principle according to the invention may be implemented regardless of the specific type of flotation, i.e. the flotation technique may be any per se known flotation technique, such as froth flotation, dissolved air flotation or induced air flotation.

The basic operating principle of the flotation device 1 is given in figures 1a-b, 2, 3 and 4 a-c. The following description should be read primarily in connection with these figures unless otherwise noted.

The first rougher primary flotation cell 111a of the primary flotation circuit 10 receives a flow of suspension, i.e., a slurry inflow 100, which includes ore particles, water, and in some cases flotation chemicals (e.g., collecting chemicals and non-collecting flotation agents) for separating the slurry into an underflow 40 and an overflow 51 a. A typical flotation cell 111, 112, 210, 300 is shown in figure 16. The flotation cell may include a mixer 78 in the form of a mechanical agitator as shown in fig. 16, or any other suitable mixer for promoting collisions between flotation bubbles and ore particles. In one embodiment, the flotation gas may be fed or introduced into a flotation tank that separates the slurry into an overflow and an underflow. In one embodiment, the flotation gas may be fed into a flotation tank section in which a mixer is arranged, i.e. into a preliminary flotation tank before the ore particles float and are thus separated into overflow and underflow.

In a flotation process where conventional flotation is carried out using flotation chemicals, a similar froth flotation process occurs: the collector chemical molecules adhere to the surface region of the ore particles with the value mineral through an adsorption process. The value mineral acts as an adsorbent and the collector chemical acts as an adsorbate. The collector chemical molecules form a film on the valuable mineral area of the surface of the ore particles. The collector chemical molecule has a non-polar portion and a polar portion. The polar part of the collector molecule adsorbs to the surface area of the ore particles with the value mineral. The non-polar moiety is hydrophobic and thus repelled by water. Repulsion causes the hydrophobic tail of the collected molecule to adhere to the flotation bubble. One example of flotation gas is air pumped to the flotation cell. Sufficient adsorption of the collector molecules onto a sufficiently large surface area of the value mineral on the ore particles can result in the ore particles adhering to the flotation bubbles. It is also contemplated that the flotation process may be conducted without flotation chemicals. The flotation process can also be carried out as reverse flotation. In the following, most of the examples are disclosed in view of conventional flotation, unless otherwise indicated the examples relate specifically to reverse flotation. However, all the examples and illustrations given can also be realized in a reverse flotation process.

The ore particles attach or adhere to the gas bubbles to form bubble-ore particle agglomerates. These agglomerates rise to the uppermost surface of the flotation tank 111, 112, 210, 300 by the buoyancy of the bubbles and the continuous upward flow of slurry that may be caused by mechanical agitation and feeding of the slurry into the flotation tank 111, 112, 210, 300.

The bubbles may form a foam layer. Froth, including bubble-ore particle agglomerates, that collects on the surface of the slurry in the flotation cell 111, 112, 210, 300 flows out of the flotation cell 111, 112, 210, 300, through the launder lip 76, and into the launder 75. It is also conceivable that the flotation cell is used as a so-called overflow flotation cell, in which no continuous cohesive froth layer is formed on the surface of the slurry, but the actual slurry floating in the flotation cell, including the ore particles of the valuable minerals, is driven to flow through the flow cell lip 76.

From the surface of the slurry at the top of the rougher primary flotation cell 111a, 111b, the value minerals containing ore particles overflow the launder lip 76 of the flotation cell and are collected in the launder 75. Of course, in the case of reverse flotation, the ore particles that do not contain valuable minerals are collected in the overflow, while the ore particles that contain valuable minerals are recovered by the underflow.

This portion of the slurry is referred to as the primary overflow 51a, 51 b. Overflow 50a, 50b is collected from the secondary flotation cells 210a, 210b in the same manner. The launder lip 76 refers here to the peripheral edge of the upper part of the flotation cell 111, 112, 210, 300, over which the froth with valuable material particles overflows to the launder 75.

The overflow 50a, 50b from the secondary flotation circuit 20 is recovered as a first concentrate 81. The first concentrate 81 of ore particles containing valuable minerals is in fluid form, which is directed to further flotation circuits or stages according to embodiments of the invention, or to other further processing according to solutions known in the art.

From the region near the flotation tank bottom 71, gangue or a portion of the slurry containing ore particles that do not rise to the surface of the slurry is drawn as underflow 40 from the rougher primary flotation tank 111 a. The underflow 40 is introduced into a subsequent rougher first flotation cell 111b which receives the underflow 40 as feed from the prior rougher first flotation cell 111 a. The slurry is treated in a subsequent rougher primary flotation cell 111b, similar to that in the first rougher primary flotation cell 111a, in a manner well known to those skilled in the art.

The primary flotation circuit 10 comprises a rougher section 11 having at least two rougher primary flotation cells 111a, 111b connected in series and arranged in fluid communication, followed by a scavenger section 12 having at least two scavenger primary flotation cells 112a, 112b connected in series and arranged in fluid communication. The last rougher primary flotation cell 111e is connected in series with the first scavenger primary flotation cell 112a and is arranged in fluid communication, so that the rougher primary flotation cell 111 of the rougher section 11 and the scavenger primary flotation cell 112 of the scavenger section 12 constitute a continuous process line. The overflow 51a from the first rougher primary flotation cell 111a may be arranged to flow directly into the secondary flotation circuit 20, 30.

Overflow 52 from the scavenger primary flotation cells 112a-d is arranged to flow back to the rougher flotation cells 111a-f (see figure 3). Alternatively, the overflow 52 from the scavenger primary flotation cells 112a-d may be arranged to flow into the regrinding step 64 and then into the scavenger concentration flotation circuit (see figures 1a, 1b, 2).

The primary overflow 52 from the at least one scavenger primary flotation cell 112 may be arranged to flow directly into the regrinding step 64. In one embodiment, the combined primary overflow from the scavenger primary flotation tank 112 of the scavenger section 12 may be arranged to flow directly into the regrinding step 64.

The primary flotation circuit 10 may comprise at least four primary flotation cells 111, 112. Alternatively, the primary flotation circuit 10 may comprise 4-10 primary flotation cells 111, 112. Alternatively, the primary flotation circuit 10 may comprise 4-7 primary flotation cells. The rougher section 11 may comprise at least two rougher primary flotation cells 111a, 111 b. Alternatively, the rougher section 11 may include 2-6 rougher primary flotation cells 111 a-f. Alternatively, the rougher section 11 may include 2-4 rougher primary flotation cells 111 a-d. The scavenger section 12 may comprise at least two scavenger primary flotation cells 112 a-b. Alternatively, the scavenger section 12 may contain 2-6 scavenger primary flotation cells 112 a-d. Alternatively, the scavenger section 12 may contain 2-4 scavenger primary flotation cells 112 a-d. Embodiments of the invention are described in the "examples" section of this disclosure, including different numbers of primary flotation cells in the primary flotation circuit 10.

The rougher and/or scavenger primary flotation cells 111a-f, 112a-d are connected in series. The fluid connection may be realized by means of a conduit 500 (pipe or tube, as shown in the figure) such that the subsequent primary flotation cells 111a-f, 112a-d are arranged at a distance from each other. Alternatively, any two adjacent or subsequent primary flotation cells 111a-f, 112a-d may be arranged in direct cell connection, so that no separate conduit (not shown in the figures) is required between the two flotation cells 111a-e, 112 a-e.

In an embodiment of the invention, in case the primary flotation circuit 10 comprises more than two rougher primary flotation cells 111a-f, all adjacent or subsequent primary flotation cells 111a-f, 112a-d may be arranged in fluid connection with the conduit 500 arranged between the flotation cells for conducting the underflow 40 from one flotation cell to the next. Alternatively, all flotation cells 111a-f, 112a-d may be arranged in direct cell connection with adjacent flotation cells. Alternatively, some adjacent flotation cells 111a-f, 112a-d may be arranged in direct cell connection with adjacent flotation cells, while other adjacent flotation cells may have conduits 500 for achieving fluid connection. The arrangement and design of the primary flotation circuit 10 may depend on the overall process requirements and physical location of the flotation device 1.

Furthermore, the first secondary flotation tank 210a of the secondary flotation circuit 20 and the further secondary flotation tank 210b of the secondary flotation circuit 20 may be arranged in direct fluid communication with the first rougher primary flotation tank 111a, 111b from which the secondary flotation tank 210a, 210b receives the overflow 51a, 51b, i.e. without further processing steps, such as grinding steps or conditioning steps arranged between the primary flotation circuit 10 and the secondary flotation circuit 20.

From the last scavenger primary flotation cell 112d of the flotation circuit 10, an underflow 40' (which may be rejected in normal flotation or acceptable in reverse flotation) is withdrawn from the flotation apparatus 1 as a tailings stream 83, which may be further processed in any suitable manner known in the art.

The first rougher primary flotation cell 111a may have a volume of at least 150m³. Alternatively, the first rougher primary flotation cell 111a may have a volume of at least 500m³. Alternatively, the first rougher primary flotation cell 111a may have a volume of at least 2000m³。

The volume of the second rougher first flotation cell 111b, or any of the subsequent rougher first flotation cells 111b-f downstream of the first rougher first flotation cell 111a, may be at least 100m³. Alternatively, the volume of the second rougher first flotation cell 111b, or any of the subsequent rougher first flotation cells 111b-f downstream of the first rougher first flotation cell 111a, may be at least 300m³. Alternatively, the volume of the second rougher first stage flotation cell 111b, or any of the subsequent rougher first stage flotation cells 111b-f downstream of the first rougher first stage flotation cell 111a, may be at least 500m³。

In an embodiment of the invention, the second primary flotation cell 111b, some of the subsequent rougher primary flotation cells 111b-f downstream of the first rougher primary flotation cell 111a, or all of the subsequent rougher primary flotation cells 111b-f downstream of the first rougher primary flotation cell 111a may have the same volume as the first rougher primary flotation cell 111a (see fig. 12). In an embodiment of the invention, the second primary flotation cell 111b, some of the subsequent rougher primary flotation cells 111b-f downstream of the first rougher primary flotation cell 111a, or all of the subsequent rougher primary flotation cells 111b-f downstream of the first rougher primary flotation cell 111a, may be smaller in volume than the first primary flotation cell 111a (see fig. 11).

The primary overflow 51a from the first rougher primary flotation tank 111a is directed to the first secondary flotation tank 210a of the secondary flotation circuit 20. The first secondary flotation tank 210a is arranged in direct fluid communication with at least one first rougher primary flotation tank 111 a. The first secondary flotation tank 210a is arranged to receive the primary overflow 51a of the at least one first rougher primary flotation tank 111a as an inflow for recovering a first concentrate 81 containing ore particles with valuable minerals. The first secondary flotation cell 210a, as well as any other secondary flotation cells, operate on standard flotation principles, as previously described in this disclosure. The overflow 50a of the first secondary flotation cell 210a is collected as the first concentrate 81, which may then be directed to any suitable further processing step known in the art.

The secondary flotation circuit 20 includes at least two secondary flotation cells 210 in fluid communication. In one embodiment, the secondary flotation circuit 20 may include 2-10 secondary flotation cells 210a-210j in fluid communication. In one embodiment, the secondary flotation circuit 20 may include 4-7 secondary flotation cells 210 a-g. In another embodiment, the secondary flotation circuit 20 may include three secondary flotation cells 210 a-c.

In the secondary flotation circuit 20, a first secondary flotation tank 210a is arranged in fluid communication with at least one rougher primary flotation tank 111a and is arranged to receive a primary overflow 51a from the at least one rougher primary flotation tank 111a for recovering the first concentrate 81. The further secondary flotation tank 210b is arranged in fluid communication with the at least one further rougher primary flotation tank 111b and is arranged to receive a primary overflow 51b from the at least one further rougher primary flotation tank 111b for recovering the first concentrate 81. The further secondary flotation cell 210b is arranged in fluid communication with the preceding secondary flotation cell 210 a.

The further secondary flotation cells 210b-c of the secondary flotation circuit 20 may be arranged in direct cell connection with each other or they may be arranged in fluid connection with each other via a conduit 500. In one embodiment, all adjacent secondary flotation cells 210a-c of the secondary flotation circuit 20 may be arranged in direct cell connection with each other; alternatively, all adjacent secondary flotation cells 210a-c may be arranged to be fluidly connected by conduit 500; alternatively, some adjacent secondary flotation cells 210a-c may be arranged in direct cell connection, while others may be arranged with conduits 500 between them, similar to that described for the primary flotation circuit 10.

In the embodiment shown in fig. 4a, the secondary underflow 42a from the first secondary flotation tank 210a can be arranged to flow to another secondary flotation tank 210 b. Alternatively, the underflow 42a from the first secondary flotation tank 210a may be arranged to be combined with the secondary underflow 42b of the further secondary flotation tank 210b (not shown in the figure).

The first secondary flotation cell 210a of the secondary flotation circuit 20 in fluid communication with the rougher primary flotation cell 111a has a volume of 100-³. Alternatively, the first secondary flotation cell 210a of the secondary flotation circuit 20 in fluid communication with the rougher primary flotation cell 111a may have a volume of 400-³。

The volume of the first secondary flotation tank 210a of the secondary flotation circuit 20 in fluid communication with the at least one rougher primary flotation tank 111a is 2-50% of the total volume of the at least one rougher primary flotation tank 111 a. Alternatively, the volume of the first secondary flotation tank 210a of the secondary flotation circuit 20 in fluid communication with the at least one rougher primary flotation tank 111a may be 3-30% of the total volume of the at least one rougher primary flotation tank 111a (see fig. 4 c).

The total volume here refers to the combined volume of the rougher primary flotation tank 111a from which the first secondary flotation tank 210a receives the overflow 51 a. For example, the first secondary flotation tank 210a may receive overflow 51a from more than one rougher primary flotation tank 111 of the primary flotation circuit 10. In this case, the total volume is the combined volume of the rougher primary flotation cells 111.

At least one further secondary flotation tank 210b is arranged downstream of the first secondary flotation tank 210 a. The further secondary flotation cell 210b is arranged in direct fluid communication with at least one further rougher primary flotation cell 111b of the primary flotation circuit 10. The further secondary flotation tank 210b of the secondary flotation circuit 20 is arranged to receive the primary overflow 51b of the at least one further rougher primary flotation tank 111 b. The further secondary flotation tank 210b is arranged to receive the primary overflow 51b of the at least one further rougher primary flotation tank 111b as an inflow for recovering the first concentrate 81 containing ore particles with valuable minerals. The further secondary flotation cell 210b, as well as any other secondary flotation cell 210, operates on standard flotation principles, as previously described in this disclosure. The overflow 50b of the secondary flotation cell 210b is collected as the first concentrate 81, which may then be directed to any suitable further processing step known in the art.

The number of secondary flotation cells 210 in series in the secondary flotation circuit 20 may be the same (equal) as the number of rougher primary flotation cells 111 in the primary flotation circuit 10. In some embodiments, the number of secondary flotation cells 210 in the secondary flotation circuit 22 may be less than the number of rougher primary flotation cells 111 in the primary flotation circuit 10.

The secondary flotation cells 210a, 210b may be arranged to receive the primary overflow 51a, 51b from 1-3 rougher primary flotation cells 111. In one embodiment, the secondary flotation tank 210a, 210b may be configured to receive the primary overflow 51a, 51b from 1-2 rougher primary flotation tanks 111a, 111 b. In one embodiment, the secondary flotation tank 210a, 210b may be arranged to receive a primary overflow 51a, 51b from at most two rougher primary flotation tanks 111a, 111 b. In one embodiment, the secondary flotation tank 210a may be arranged to receive a primary overflow 51a from one rougher primary flotation tank 111 a.

Alternatively or additionally, the further secondary flotation tank 210b may be arranged to receive a primary overflow 51b, 51c from at least two rougher primary flotation tanks 111b, 111c (see fig. 12). The further secondary flotation tank 210b may be arranged to receive a primary overflow 51b-d from 1-4 rougher primary flotation tanks 111 b-d. In one embodiment, the further secondary flotation tank 210b may be arranged to receive a primary overflow 51b-d from 1-2 rougher primary flotation tanks 110 b-c. For example, an embodiment in which the further secondary flotation cell 210b receives a primary overflow 51b from one rougher primary flotation cell 111b is shown in fig. 1a-1 b and 2.

The underflow 42b from the further secondary flotation cell 210b may be arranged to flow back to the rougher section 11 of the primary flotation circuit 10 at a point downstream of the rougher primary flotation cell 111b from which the further secondary flotation cell 210b receives the overflow 51b (see fig. 1 a). In one embodiment, the underflow 42b flowing from the further secondary flotation cell 210b is arranged to flow back to the further rougher primary flotation cell 110c downstream of the first rougher primary flotation cell 111b from which the further secondary flotation cell 210b receives the primary overflow 51b (see fig. 6a, 9). In one embodiment, the underflow 42b flowing from the further secondary flotation cell 210b is arranged to be combined into an overflow 51 flowing from at least one further rougher primary flotation cell 111c downstream of the rougher primary flotation cell 111b from which the further secondary flotation cell 210b receives a primary overflow 51b (see fig. 1 b).

In one embodiment, the underflow 42c from the last additional secondary flotation tank 210c of the secondary flotation circuit 20 can be arranged to be combined with the overflow 52a of the scavenger primary flotation tank 112a, or with the combined overflow 52a-d of two or more scavenger primary flotation tanks 112a-d of the scavenger section 12, as shown in figure 2 (solid line). This is because the quality in terms of the amount of valuable mineral particles still present in the underflow 42c is close to or similar to the quality of the overflow 52 of the scavenging line 12, so that both streams can be directed to further processing, for example, to be reground 64 together. This may increase the efficiency of the flotation device 1 and may also save energy consumption, since the number of individual further processing steps may be reduced.

Alternatively, depending on the mineral composition of the underflow 42c, it may also be introduced into the scavenger section 12 of the flotation apparatus 1 for scavenger flotation treatment. The underflow 42c can be introduced into the scavenger first flotation cell 112a either directly into the flotation cell or into a conduit between the two first flotation cells 111, 112. In fig. 2 an embodiment is shown in which the underflow 42c is introduced into the conduit between the last rougher first stage flotation cell 111e and the first scavenger first stage flotation cell 112a to be combined (dashed line) with the underflow 40 of the rougher section 11. It is contemplated that the underflow 42c may also be introduced into a conduit between any two scavenger primary flotation cells 112a-d for treatment in the scavenger primary flotation cell. The above embodiment is particularly beneficial if the quality of the underflow 42c from the secondary flotation circuit 20 is such that it requires further flotation in order to efficiently recover valuable mineral particles from the slurry stream.

And a rougher primary flotation cell 111 (e.g. of the typePrimary flotation cell 111b) another secondary flotation cell 210b of the secondary flotation circuit 20 in direct fluid communication has a volume of 100-³. Alternatively, the volume of the other secondary flotation cell 210b of the secondary flotation circuit 20 in direct fluid communication with the rougher primary flotation cell 111 (e.g., primary flotation cell 111b) may be 300-³。

The volume of the other secondary flotation cell 210b of the secondary flotation circuit 20 in fluid communication with the at least one rougher primary flotation cell 111 is 2-50% of the total volume of the at least one primary flotation cell 111. Alternatively, the volume of the further secondary flotation cell 210b of the secondary flotation circuit 20 in fluid communication with the at least one rougher primary flotation cell 111 is 3-30% of the total volume of the at least one primary flotation cell 111 (see fig. 4 c).

The total volume here refers to the total volume of each primary flotation cell 111 from which the secondary flotation cell 210b receives the overflow 51. For example, another secondary flotation cell 210b may receive overflow 51b, 51c from the primary flotation cells 111b, 111c of the primary flotation circuit 10 (see fig. 12). In this case, the total volume is the total volume of each primary flotation cell 111b, 111 c.

In one embodiment, the first secondary flotation tank 210a of the secondary flotation circuit 20 has a larger volume than the other secondary flotation tank 210b of the secondary circuit 20.

In one embodiment, the volume of the other secondary flotation tank 210b of the secondary flotation circuit 20 is greater than the volume of the first flotation tank 210a of the secondary flotation circuit 20.

Subsequent further secondary flotation cells 210b, 210c of the secondary flotation circuit 20 may be arranged in direct cell connection with each other or they may be arranged in fluid connection with each other through a conduit 500. In one embodiment, all adjacent secondary flotation cells 210 of the secondary flotation circuit 20 may be arranged in direct cell connection with each other; alternatively, all adjacent secondary flotation cells 210 may be arranged to be fluidly connected by a conduit 500; alternatively, some adjacent secondary flotation cells 210 may be arranged in direct cell connection, while others may be arranged with conduits 500 between them, similar to that described for the primary flotation circuit 10.

From the region near the flotation tank bottom 71, gangue or a portion of the slurry containing ore particles that do not rise to the surface of the slurry is directed as underflow 42a from the first secondary flotation tank 210 a. The underflow 42a is introduced into another or subsequent secondary flotation tank 210b, which secondary flotation tank 210b receives the underflow 42a as feed from the previous secondary flotation tank 210 a. Similar to the first secondary flotation cell 210a, the slurry is processed in another or a subsequent secondary flotation cell 210b in a manner well known to those skilled in the art.

In one embodiment, the underflow 42b from the further secondary flotation tank 210b is arranged to flow to the last rougher primary flotation tank 111 of the at least one rougher primary flotation tank 111 from which the primary overflow 51b is received, or to the rougher primary flotation tank 110c (see fig. 6a-c, 9) downstream of the last rougher primary flotation tank 111b of the at least one rougher primary flotation tank 111 from which the primary overflow 51b is received. The underflow 42b may be directed into a conduit 500 (see fig. 1b) before the rougher first flotation cell 111 to which the underflow 42b is directed, or into a collecting conduit 510 (see fig. 1a) for collecting overflow from a plurality of rougher first flotation cells 111, or directly into a rougher first flotation cell (see, e.g., fig. 6 a).

In one embodiment, the underflow 42' from the last secondary flotation cell of the secondary flotation circuit 20 may be arranged to flow out of the other secondary flotation cell 210b as tailings stream 83.

In one embodiment, the underflow 42b may be arranged to flow to a rougher primary flotation tank 111c downstream of the rougher primary flotation tank 111b from which the primary overflow 51b is received. The underflow 42b can be arranged to flow directly into the rougher first flotation cell 111b, 111c or into the conduit 500 before the rougher first flotation cell 111b, 111 c.

In one embodiment, the primary overflow 51a from the primary flotation tank 111a may be arranged to flow into two parallel secondary flotation tanks 210 a. This embodiment is not shown in the figures. For example, such an embodiment may be easily imagined in the embodiment shown in fig. 5 a: a second first secondary flotation tank 210a is arranged beside or near a single secondary flotation tank 210a in the secondary flotation circuit 20 and the overflow 51a is led via a collecting duct 510 into two parallel secondary flotation tanks 210 a. The first concentrate 81 as overflow 50a from the two parallel first secondary flotation cells 210a will be collected separately and directed further, while the underflow 42 from the two parallel first secondary flotation cells 210a can be collected via a collecting duct 510 similar to that shown for example in fig. 7 and directed downstream to the other secondary flotation cell 210 b.

The slurry stream, underflow 40, 42 and overflow 50, 51, 52 may be arranged to be driven by gravity. That is, any flow between any at least two flotation cells that are fluidly connected may be driven by gravity. For example, the flow of slurry between the first rougher primary flotation cell 111a and the further rougher primary flotation cell 111b may be driven by gravity. Alternatively or additionally, the flow of slurry between the first scavenger first flotation cell 112a and the further scavenger first flotation cell 112b may be driven by gravity. Alternatively or additionally, the flow of slurry between the rougher primary flotation cell 111e and the scavenger flotation cell 112a may be driven by gravity. Alternatively or additionally, the flow of slurry between the first secondary flotation cell 210a and the further secondary flotation cell 210b may be driven by gravity. Alternatively or additionally, the flow of slurry between the rougher primary flotation cell and the secondary flotation cell, which are fluidly connected to each other, may be driven by gravity. For example, the flow of slurry between the first rougher primary flotation cell 111a of the primary flotation circuit 10 and the first secondary flotation cell 210a of the secondary flotation circuit 20 may be driven by gravity. For example, the flow of slurry between the other rougher primary flotation cell 111b of the primary flotation circuit 10 and the other secondary flotation cell 210b of the secondary flotation circuit 20 may be driven by gravity.

In order to promote the gravitational movement of the slurry flow, at least some of the flotation cells 111, 112, 210, 300 may be arranged in a step-like arrangement with respect to the ground on which the flotation device is placed (see fig. 5c and 6 c). Alternatively, the launder lips 76 of each flotation cell (e.g., primary flotation cells 111a-c) may be arranged at different heights.

As can be seen in fig. 5c and 6c, the step between any adjacent flotation cells results in a difference in the level 70 of the slurry surface of two adjacent flotation cells. In this case, the steps are arranged between the rougher primary flotation cells 111 of the primary flotation circuit 10 and between the two secondary flotation cells 210a, 210b of the secondary flotation circuit 20. It is also envisaged that a step may be arranged between the rougher primary flotation cell 111 of the primary flotation circuit and at least one secondary flotation cell 210a or another secondary flotation cell 210b of the secondary flotation circuit 20; alternatively, between adjacent secondary flotation cells 210a, 210b of the secondary flotation circuit 20; or between the last rougher primary flotation cell 111e and the first scavenger primary flotation cell 112 a; or between two scavenger primary flotation cells 112 of the scavenger section 12 of the primary flotation circuit 10.

It is obvious to the person skilled in the art that the vertical positioning of the different flotation cells 111, 112, 210, 300 can be achieved in the best possible way, taking into account the requirements of the flotation process and the construction site of the flotation device 1.

The gravity flow of the slurry is achieved by a hydraulic gradient between any two flotation cells having different slurry surface heights, by a step between the flotation cell bottoms 71 as shown in figures 5c and 6c, or a step between the cell lip heights, as already explained before in the summary section of the present disclosure.

Alternatively or additionally to the above-described manner of gravity-driven slurry flow, the slurry flow may be driven by one or more low-lift pumps arranged between any two adjacent flotation cells in the case of flotation cells of the same architecture, either into the conduit 500 or directly between adjacent flotation cells in the case where adjacent flotation cells are directly cell-connected to each other. Pumping is required when the or each cell is arranged in a co-planar manner (i.e. the bottom 71 of each cell is at a single level relative to the ground), whereby the pulp surface heights of two adjacent cells will be approximately the same and whereby the resulting hydraulic gradient is at least insufficient to drive the pulp flow by gravity. In one embodiment, in the flotation apparatus 1, the flow of slurry may be driven by gravity between some adjacent flotation cells and by a low-lift pump between some adjacent flotation cells.

The flotation device 1 may also comprise a further processing step 62. For example, the overflow 51c of at least one rougher primary flotation cell 111c may be directed to flow into the further process step 62. In one embodiment, the combined overflow of the at least one rougher primary flotation cell 111c and the overflow of the at least one further rougher primary flotation cell 111d downstream of the rougher primary flotation cell 111c may be directed to flow into the further processing step 62. In fig. 15, a flotation device 1b is shown, in which the overflow 51c, 51d of the above-described rougher primary flotation cells 111c, 111d of the primary flotation circuit 10b is combined and led via a collecting duct 510 to a further process step 62. Another process step 62 in this embodiment is concentration flotation performed on a concentration flotation circuit.

Alternatively or additionally, the combined secondary overflow 50a, 50b of the at least two secondary flotation cells 210a, 210b may be arranged to flow into a further process step 62.

The underflow 40' from the last flotation cell of the primary flotation circuit 10 (i.e. the last scavenger primary flotation cell 112d) may be arranged to flow into a further treatment step 62 or may be arranged to leave the flotation apparatus 1 as tailings 83. Alternatively or additionally, the underflow 42' from the last secondary flotation tank 210b of the secondary flotation circuit 20 may be arranged to flow into another processing step 62 or may be arranged to leave the flotation apparatus 1 as tailings 83.

Another processing step 62 may include, for example, a grinding step. Alternatively or additionally, another processing step 62 may include an adjustment step. Alternatively or additionally, another processing step 62 may include a flotation step, such as a concentration flotation step. In other words, the further processing step 62 may also comprise a plurality of individual processing steps in combination.

The flotation apparatus 1 may further comprise an additional secondary flotation circuit 30, the secondary flotation circuit 30 comprising at least one additional secondary flotation cell 300 in fluid communication with at least one rougher primary flotation cell 111 and arranged to receive a primary overflow 51 from at least one other rougher primary flotation cell 111 (see e.g. fig. 7 and 8). The additional secondary flotation cell 300 operates in substantially the same manner as the other secondary flotation cells 210, as previously described herein.

The additional secondary flotation tank 300 is arranged to receive the primary overflow 51b of at least one rougher primary flotation tank 111 and the underflow 42 from another secondary flotation tank 210 b. The underflow 42' from the additional secondary flotation tank 300 is arranged to leave the flotation device 1 as tailings stream 83. Alternatively or additionally, the underflow 42' from the additional secondary flotation tank 300 may be directed to another processing step 62.

In one embodiment, the first secondary flotation tank 210a may be arranged to receive a primary overflow 51a from the first rougher primary flotation tank 111a, and the additional secondary flotation tank 300 is arranged to receive primary overflows 51b, 51c from at least two further rougher primary flotation tanks 111.

In an embodiment, the additional secondary flotation tank 300 may be arranged to receive a primary overflow 51b, 51c of at least two rougher primary flotation tanks 110b, 110c (this embodiment is not shown in the figures). In one embodiment, the additional secondary flotation tank 300 may be a conventional concentration tank 300 arranged to receive the primary overflow 51c, 51d, 51e of at least three rougher primary flotation tanks 111c, 111d, 111e (see, e.g., fig. 9).

In one embodiment, an additional secondary flotation tank 300 may be arranged in a position downstream of the at least one first secondary flotation tank 210a and/or the at least another secondary flotation tank 210b (see e.g. fig. 7, 8 and 10).

According to one embodiment of the invention, the flotation device 1 may comprise two primary flotation circuits 10a, 10 b. The first secondary flotation tank 210a of the secondary circuit 20 may receive overflow 51a, 52a from the first rougher primary flotation tanks 111a, 121a of the two primary flotation circuits 10a, 10b (see fig. 13). In one embodiment, the secondary flotation circuit 20 may comprise two additional secondary flotation tanks 300a, 300b arranged to receive a combined overflow from the further rougher primary flotation tanks 111b-e and 121b-e of the two primary flotation circuits 10a, 10b, respectively. The secondary underflow 42 from the first secondary flotation tank 210a can be arranged to flow to two additional secondary flotation tanks 300a, 300b as shown in figure 13. Similarly to what has been described above, the underflow 42' can be arranged to flow into a further treatment step 62, either separately or else in combination; or arranged to leave the flotation apparatus 1 as tailings 83 from two additional secondary flotation cells 300a, 300b, respectively. The tailings streams 83 of the additional secondary flotation cells 300a, 300b can also be combined and then leave the flotation device as a combined tailings stream 83.

The at least one rougher primary flotation cell 111a-f and/or the at least one secondary flotation cell 210a-b, 300 may comprise a froth flotation cell, or a so-called conventional flotation cell, the operation of which has been described in the summary section of the present disclosure. In one embodiment, the third rougher primary flotation cell 111c of the primary flotation circuit 10 comprises a froth flotation cell. Additionally, any subsequent rougher primary flotation cells 111d-f after the third rougher primary flotation cell 111c may include froth flotation cells. In one embodiment, the first rougher primary flotation cell 111a and the second rougher primary flotation cell 111b of the primary flotation circuit 10 may operate as overflow flotation cells, the details of which have also been described in the summary section of the present disclosure.

Alternatively or additionally to both embodiments described above, the secondary flotation circuit 20 may comprise at least one concentration cell, i.e. one or more secondary flotation cells 210a-b, 300 may be used as a rougher concentration cell, so that the secondary flotation circuit 20 may be understood as, or operated in the manner of, a rougher concentration circuit or circuit.

In one embodiment, the flotation gas may be fed into a flotation tank that separates the slurry into an overflow and an underflow. The flotation cell into which the flotation gas is fed may comprise a mixer. Alternatively, the flotation gas may be fed into a prefloat cell 115 in which a mixer is arranged.

The flotation apparatus 1 described herein is particularly suitable for, but not limited to, use in the recovery of value mineral containing ores in which the mineral ore particles comprise copper (Cu), zinc (Zn), iron (Fe), pyrite or metal sulphides (e.g. gold sulphides). Mineral ore particles containing other valuable minerals (e.g., Pb, Pt, PGMs (platinum group metals Ru, Rh, Pd, Os, Ir, Pt), oxide minerals, industrial minerals (e.g., Li (i.e., spodumene), petalite), and rare earth minerals may also be recovered according to various aspects of the present invention.

An embodiment of the use of the flotation device according to the invention makes it possible to use a volume of at least 150m in the flotation device³And gravity driven slurry flow. An embodiment of the use of the flotation device according to the invention makes it possible to use a volume of at least 500m in the flotation device³And gravity driven slurry flow. An embodiment of the use of the flotation device according to the invention makes it possible to use a volume of at least 2000m in the flotation device³And gravity driven slurry flow.

An embodiment of a use of the flotation device according to the invention can alternatively or additionally be used with a volume of at least 100m³And gravity is used to drive the slurry stream. An embodiment of the use of the flotation device according to the invention can use a volume of at least 300m³And gravity is used to drive the slurry stream. An embodiment of the use of the flotation device according to the invention can use a volume of at least 500m³And gravity is used to drive the slurry stream.

An embodiment of the use of the flotation device according to the invention may alternatively or additionally use gravity to drive the flow of slurry between the rougher primary flotation cells 111 a-f.

An embodiment of the use of the flotation device according to the invention can alternatively or additionally use gravity to drive the flow of slurry between the secondary flotation cells 210a-b, 300.

An embodiment of the use of the flotation device according to the invention may alternatively or additionally use gravity to drive the flow of slurry between the rougher primary flotation cell 111 and the secondary flotation cell 210, which are fluidly connected to each other. An embodiment of the use of the flotation device according to the invention can use gravity to drive the flow of slurry between the first rougher primary flotation cell 111a and the first secondary flotation cell 210 a. Alternatively or additionally, another embodiment of the use of the flotation device according to the invention may use gravity to drive the flow of slurry between the further rougher primary flotation cell 110b-f and the further secondary flotation cell 210b or the additional secondary flotation cell 300.

According to another aspect of the invention, the flotation system 9 comprises a flotation device 1 according to the present description. In one embodiment, the flotation system 9 may comprise at least two flotation devices 1. In one embodiment, the flotation system 9 may comprise at least three flotation devices 1. In one embodiment, the flotation system 9 may comprise at least one first flotation device 1a for recovering a first concentrate 81 and at least one second flotation device 1b for recovering a second concentrate 82 (see fig. 15).

In one embodiment, the primary flotation cells 111, 112 of the primary flotation circuit 10a of the at least one first flotation device 1a for recovering the first concentrate 81 and the primary flotation cells 111, 122 of the primary flotation circuit 10b of the at least one second flotation device 1b for recovering the second concentrate 82 are arranged in series (see fig. 15).

The flotation system 9 may comprise a flotation device 1 arranged to recover Cu. Alternatively or additionally, the flotation system 9 may comprise a flotation device 1 arranged for recovering Zn, alternatively or additionally, the flotation system 9 may comprise a flotation device 1 arranged to recover pyrite. Alternatively or additionally, the flotation system 9 may comprise a flotation device 1 arranged to recover metal (e.g. gold) from sulphides. According to another embodiment of the invention, the flotation system 9 may comprise a flotation device 1 arranged to recover mineral ore particles containing Cu from low grade ore. According to one embodiment of the invention the flotation system 9 may comprise a flotation device 1 arranged to recover Fe by reverse flotation.

The flotation system 9 may also include means for further processing the mineral ore particles suspended in the slurry so that the second concentrate 82 is different from the first concentrate 81. In one embodiment, the means for further processing of the mineral ore particles may be a grinding step 62 arranged between the first flotation device 1a and the second flotation device 1 b. In one embodiment, the means for further processing of mineral ore particles may be a means 65 for adding flotation chemicals arranged between the first flotation device 1a and the second flotation device 1 b.

According to another aspect of the present invention, a flotation method for treating mineral ore particles suspended in a slurry is presented. In the process, the slurry is subjected to a first stage flotation 10 comprising at least two rougher flotation stages 111a, 111b in series and in fluid communication to separate the slurry into a first underflow 40 and a first overflow 51a, 51b, and further comprising at least two scavenger flotation stages 112a, 112b in series and in fluid communication to separate the slurry into an underflow 40 and a first overflow 52a, 52 b.

The primary underflow 40 from the preceding stage 111a can be directed to the subsequent stage 111 b. The primary overflow 51a from the at least first primary flotation stage 110a is led to a first secondary flotation stage 210a of the secondary flotation 20 for recovering the first concentrate 81, the secondary flotation 20 comprising at least two secondary flotation stages 210a, 201b in series and in fluid communication. At least a first rougher flotation stage 110a and a first secondary flotation stage 210a are arranged in series and in fluid communication. Furthermore, according to the method, in the secondary flotation 20, the primary overflow 51b from at least one further rougher flotation stage 111b is directed to a further secondary flotation stage 210b arranged in series and in fluid communication with the at least one further rougher flotation stage 111b to recover the first concentrate 81, and the underflow 42a from the preceding secondary flotation stage 210a is directed to the further secondary flotation stage 210 b. Alternatively, the underflow 42a from a previous secondary flotation stage 210a may be combined with the underflow 42b from another secondary flotation stage 210 b. The primary overflow 52a, 52b from the scavenger flotation stages 112a, 112b is directed back to the rougher flotation stages 111a, 111b or to regrind 64 and then to cleaner flotation.

The slurry may be subjected to at least four primary flotation stages. In one embodiment, the slurry may be subjected to 4-10 primary flotation stages. In one embodiment, the slurry may be subjected to 4-7 primary flotation stages. Alternatively or additionally, the slurry may be subjected to at least two secondary flotation stages. In one embodiment, the slurry may be subjected to 2-10 secondary flotation stages. In one embodiment, the slurry may be subjected to 4-7 flotation stages.

In one embodiment, the primary overflow 51c-e from 1-3 rougher flotation stages 111c-e may be directed to the secondary flotation stage 210 b. In one embodiment, the primary overflow 51b-c from 1-2 rougher flotation stages 111b-c may be directed to the secondary flotation stage 210 b. In one embodiment, the primary overflow 51c from the at least one further rougher flotation stage 111c and the secondary underflow 42 from the further secondary flotation stage 210b may be directed to an additional secondary flotation stage 300 of the secondary flotation. In one embodiment, the primary overflow 51a from the first rougher flotation stage 111a may be directed to the first secondary flotation stage 210a, and the primary overflows 51b-c from at least two further rougher flotation stages 110b-c may be directed to an additional secondary flotation stage 300.

In one embodiment, the secondary flotation stage 210a may receive a primary overflow 51a, 51b from at most two rougher flotation stages 111a, 111 b. In another embodiment, the secondary flotation stage 210a may receive the primary overflow 51a from only one rougher flotation stage 111 a. In one embodiment, the further secondary stage 210b may alternatively or additionally receive a primary overflow 51b, 51c from at most two rougher flotation stages 110b, 110 c.

In one embodiment, the underflow 42b from the secondary flotation stage 210b may be directed to the last rougher flotation stage in the at least one rougher flotation stage 111b from which the primary overflow 51b is received of the primary flotation 10, or to a rougher flotation stage 111c-e downstream of the last rougher flotation stage in the at least one rougher flotation stage 111b from which the primary overflow 51b is received.

Froth flotation may be employed in the at least one rougher flotation stage 111a and/or the at least one secondary flotation stage 210 a. Alternatively or additionally, overflow flotation may be employed in the first rougher flotation stage 111 a. In one embodiment, overflow flotation may be employed in the first rougher flotation stage 111a and the second rougher flotation stage 111 b.

Examples of the invention

The flow of slurry (overflow, underflow) between the different flotation cells (primary and/or secondary) can be arranged in any suitable manner depending on the flotation process requirements and the physical characteristics of the site where the flotation device is located. In the following, examples of possible embodiments are given.

Examples 1-10 describe in more detail the flow of slurry in and between the rougher section 11 of the primary flotation circuit 10 and the secondary flotation circuit 20, i.e. the section of the flotation apparatus 1 marked "B" in fig. 1 a. Example 11 describes a flotation system 9 according to the invention.

It will be apparent to those skilled in the art that other combinations are possible within the scope of the invention. Different embodiments may be combined to obtain a suitable arrangement. Hereinafter, embodiments of the present invention are given in conjunction with the accompanying drawings.

Example 1

In one embodiment of the invention, as shown in fig. 5a-c, a slurry inflow 100 is introduced into a flotation apparatus 1, which flotation apparatus 1 comprises a primary flotation circuit 10 having a first rougher primary flotation cell 111a for separation into an underflow 40 and an overflow 51 a. For the sake of clarity, in fig. 5a-c only part B of the whole flotation device 1 is shown.

The underflow 40 from the first rougher primary flotation tank 111a (which may include a quantity of mineral ore particles containing valuable minerals) is directed via conduit 500 into an adjacent second rougher primary flotation tank 111b connected in series with the first rougher primary flotation tank 111a for further separation into an underflow 40 and overflow 51 b.

The underflow 40 from the second rougher first flotation cell 111b (which may still include a quantity of mineral ore particles containing valuable minerals) is directed through conduit 500 to an adjacent third rougher first flotation cell 111c connected in series with the second rougher first flotation cell 111b for further separation into an underflow 40 and overflow 51 c.

It will be appreciated that after the last rougher primary flotation cell 111c shown in the figure, the underflow 40 is directed to another primary flotation cell, which may be another rougher primary flotation cell 111 or may be a scavenger primary flotation cell 112; also, after the last secondary flotation cell 210b shown in the figure, the underflow 42b is directed to the primary flotation circuit 10, to another secondary flotation cell 210, or to an additional secondary flotation cell 300 according to the invention as previously described. This applies to all examples provided herein.

The overflow 51c is collected as a first concentrate 81 for further processing in any suitable manner known in the art. The arrangement to date is typical of conventional froth flotation.

The overflow 51a from the first rougher flotation cell 111a is directed via conduit 500 into the secondary flotation circuit 20 including the secondary flotation cell 210a for separation into an overflow 50a and an underflow 42a in the secondary flotation cell 210 a. The overflow 50a is directed out of the secondary flotation circuit 20 as a first concentrate 81 for further processing in any suitable manner. This part of the flotation circuit is similar to any conventional froth flotation device.

However, in contrast to a conventional cascaded flotation process, the underflow 42a from the first secondary flotation cell 210a (which may include a quantity of mineral ore particles containing valuable minerals) is directed into another secondary flotation cell 210b for further processing to recover any remaining mineral ore particles containing valuable minerals to enhance the recovery of such minerals within the flotation apparatus 1. This is very advantageous in the recovery of ore particles containing value minerals from a slurry containing low grade ore.

Similarly, the overflow 51b from the second rougher primary flotation cell 111b is directed via conduit 500 to the secondary flotation circuit 20, more specifically to another secondary flotation cell 210b, for separation into an overflow 50b and an underflow 42b in the secondary flotation cell 210 b. The overflow 50b is directed out of the secondary flotation circuit 20 as a first concentrate 81 for further processing in any suitable manner. The concentrates 81 from the secondary flotation circuit 20 may be combined before further processing.

The underflow 42b from another secondary flotation cell 210b may be further directed in the manner described above.

The rougher primary flotation cells 111a, 111b and 111c are arranged in a step-wise manner such that there is a difference in the slurry surface level 70 between each subsequent rougher primary flotation cell 111a, 111b, 111 c. In this particular example, as shown in fig. 5c, each subsequent rougher primary flotation cell 111b, 111c has a bottom 71 arranged lower than the preceding rougher primary flotation cell 111a, 111b, thereby forming a step between the flotation cells. Of course, the difference in the pulp surface level 70 can be achieved by arranging the launder lips 76 of each subsequent rougher primary flotation cell 111a, 111b, 111c at different heights.

Also, similar steps may be provided between the secondary flotation cells 210a, 210b, between the first rougher primary flotation cell 111a and the secondary flotation cell 210a, and between the second rougher primary flotation cell 111b and the secondary flotation cell 210 b.

Due to these steps, the pulp surface height 70 of each subsequent downstream flotation cell in the direction of pulp flow is lower than the pulp surface height 70 of the preceding flotation cell, so that a suitable pressure difference is created between the cells to allow the pulp flow to be driven by gravity. This may save energy consumption since no pumping energy is required. The construction of the flotation device can also be simplified.

Example 2

In fig. 6a-c a detail B of another embodiment of the flotation device 1 is shown. In an otherwise similar embodiment to example 1, the secondary flotation cells 210a, 210b have a smaller volume than the rougher primary flotation cells 111a, 111b, 111c, and the underflow 42b from the other secondary flotation cell 210b is arranged to flow into the third rougher primary flotation cell 111c for treatment again in the rougher section 11 of the primary flotation circuit 10.

By making the secondary flotation cell smaller in volume than the rougher primary flotation cell from which it receives the overflow 51, the secondary flotation circuit 20 can more efficiently recover particles containing fewer valuable minerals (i.e. more difficult to direct to the surface froth layer and thus difficult to recover into the overflow), resulting in a higher grade concentrate 81. This will further improve the recovery of the flotation device 1.

In contrast to a conventional cascaded flotation process, the underflow 42b from the other secondary flotation cell 210b (which may still contain a certain amount of mineral ore particles containing valuable minerals) is directed into the third rougher primary flotation cell 111c for further processing in order to recover any remaining mineral ore particles containing valuable minerals, thereby improving the recovery of such minerals within the flotation apparatus 1. This so-called short circuit flotation is very advantageous for recovering ore particles containing valuable minerals from a slurry containing low grade ore.

Example 3

In one embodiment of the flotation apparatus 1, shown in detail B in fig. 7, the slurry inflow 100 is introduced into the rougher section 11 of the primary flotation circuit of the flotation apparatus, which includes a first rougher primary flotation cell 111a, for separation into an underflow 40 and an overflow 51 a.

The underflow 40 from the first rougher primary flotation tank 111a (which may include a quantity of mineral ore particles containing valuable minerals) is directed via conduit 500 into an adjacent second rougher primary flotation tank 111b connected in series with the first rougher primary flotation tank 111a, further divided into underflow 40 and overflow 51 b.

The underflow 40 from the second rougher first flotation cell 111b (which may still include a quantity of mineral ore particles containing valuable minerals) is directed through conduit 500 into an adjacent third rougher first flotation cell 111c connected in series with the second rougher first flotation cell 111b for further separation into an underflow 40 and overflow 51 c.

The underflow 40 from the third rougher first flotation cell 111c (which may still include a quantity of mineral ore particles containing valuable minerals) is directed through conduit 500 into an adjacent fourth rougher first flotation cell 111d connected in series with the third rougher first flotation cell 111c, further divided into underflow 40 and overflow 51 d.

The underflow 40 from the fourth rougher first flotation tank 111d (which may still include a quantity of mineral ore particles including valuable minerals) is directed through conduit 500 into an adjacent fifth rougher first flotation tank 111e connected in series with the fourth rougher first flotation tank 111d for further separation into an underflow 40 and overflow 51 e.

The underflow 40 from the fifth rougher primary flotation cell 111e is directed to another primary flotation cell in the primary flotation circuit 10, which may be another rougher flotation cell 111 in the scavenger section 12 of the primary flotation circuit 10 that scavenges the primary flotation cell 112.

The overflow 51a from the first rougher first flotation cell 111a is introduced via conduit 500 into the secondary flotation circuit 20 with the first secondary flotation cell 210a to separate into an overflow 50a and an underflow 42a in the first secondary flotation cell 210 a. The volume of the secondary flotation tank 210a may be less than the volume of the first rougher primary flotation tank 111 a. The overflow 50a is directed out of the secondary flotation circuit 20 as a first concentrate 81 for further processing in any suitable manner.

The underflow 42a from the first secondary flotation tank 210a, which may include a quantity of mineral ore particles containing valuable minerals, is directed to an additional secondary flotation tank 300 for further processing to recover any remaining mineral ore particles containing valuable minerals, thus increasing the recovery of that mineral within the flotation apparatus 1. The underflow 42a can be directed forward by gravity alone or, as shown in fig. 7, by a low-lift pump 60, both of which can reduce the energy consumption of the flotation process.

The overflow 51b, 51c, 51d, 51e from the further rougher primary flotation cell 111b, 111c, 111d, 111e is first collected in a collecting duct 510 and is conducted together as one inflow into the additional secondary flotation cell 300 to be separated into an overflow 50 and an underflow 42'.

The underflow 42' is arranged to flow out of the secondary flotation circuit 20 as tailings 83. The overflow 50 is directed out of the additional secondary flotation cell 300 as a first concentrate 81 for further processing in any suitable manner. The concentrate 81 from the secondary flotation circuit 20 can be combined for further processing.

The volume of the additional secondary flotation cell is selected to accommodate the total volume of overflow 51b, 51c, 51d, 51e from the rougher section 11 of the primary flotation circuit 10 and underflow 42a from the first secondary flotation cell 210 a. However, it may be smaller than the total volume of the rougher primary flotation cells 111b, 111c, 111d, 111 e.

As previously described, the rougher primary flotation cells 111a, 111b, 111c, 111d, and 111e are arranged in a stepped manner. Similarly, the secondary flotation tank 210a is one step higher than the rougher primary flotation tank 111b to which the underflow 42a is directed. There are also steps between the additional secondary flotation cell 300 and at least some of the rougher primary flotation cells 111b, 111c, 111 d. Thus, gravity can be used to drive the flow of slurry between these flotation cells.

In cases where it is not possible to arrange the different flotation cells in a stepwise manner, or only partly where it is possible, one or more low-head pumps 60 may be used to drive the flow of slurry between any two flotation cells that are in fluid connection with each other but where the difference in the respective slurry surface heights is not sufficient to allow the slurry flow to be driven by gravity alone.

Example 4

In fig. 8, an embodiment is shown which differs slightly from the one given above. The underflow 42a from the first secondary flotation cell 210a is directed to another secondary flotation cell 210b, which secondary flotation cell 210b also receives the primary overflow 51b from the second rougher primary flotation cell 111 b. From the other secondary flotation cell 210b, the underflow 42b is directed to an additional secondary flotation cell 300, which receives the overflow 51 from the rougher section 11 of the primary flotation circuit 10, although the overflow 51 is received from only three rougher primary flotation cells 111c, 111d, 111 e. Otherwise, the process operates similarly to example 3.

Example 5

The embodiment shown in fig. 9 combines the advantageous configurations of fig. 6a and 5: the rougher section 11 of the primary flotation circuit 10 includes five rougher primary flotation cells 110a-e connected in series and the treatment of the underflow 40 is similar to examples 3 and 4. The secondary flotation circuit 20 is similar to that of example 4 with a first secondary flotation cell 210a receiving an overflow 51a from the first rougher primary flotation cell 111a and a further secondary flotation cell 210b receiving a primary overflow 51b from a further rougher primary flotation cell 111b and a second underflow 42a from the first secondary flotation cell 210 a.

However, in contrast to the embodiment in example 4, the underflow 42b from the other secondary flotation tank 210b is arranged to flow back into the rougher section 10, more specifically into the third rougher primary flotation tank 111 c. It is also contemplated that the underflow 42b can be directed to a conduit 500 between the second rougher first stage flotation cell 111b and the third rougher first stage flotation cell 111c to combine with the underflow 40 of the second rougher first stage flotation cell 111b (see fig. 1 b). As previously described, the overflow 50a, 50b is collected as the first concentrate 81.

By directing the underflow 42b, which may still include a certain amount of mineral ore particles containing valuable minerals, from the further secondary flotation cell 210b back to the rougher section 11 of the primary flotation circuit 10, more particularly to the third rougher primary flotation cell 111c for further processing, any remaining mineral ore particles containing valuable minerals can be efficiently recovered, thereby increasing the recovery of such minerals within the flotation apparatus 1.

In addition, an additional secondary flotation tank 300 is provided to receive overflow 51c, 51d, 51e from the third, fourth and fifth rougher primary flotation tanks 111c, 111d, 111 e. These primary overflow streams 51c-e are first collected in a collection conduit 510 and directed as an inflow to an additional secondary flotation tank 300 for separation into overflow stream 50 and underflow stream 42'.

As mentioned above, the volume of the first and further secondary flotation cells 210a, 210b may be smaller than the volume of the rougher primary flotation cells 111a, 111 b. The volume of the additional secondary flotation tank 300 is selected to accommodate the total volume of the overflow 51c, 51d, 51 e. However, its volume may be less than the total volume of the rougher primary flotation cells 111c, 111d, 111 e.

The flow of slurry may be driven by one or more low-lift pumps, while the other flows may be driven by gravity (not shown in fig. 9) if suitable steps are arranged between adjacent flotation cells fluidly connected to each other.

The overflow 50 is directed out of the additional secondary flotation cell 300 as a first concentrate 81 for further processing in any suitable manner. The concentrate 81 from the secondary flotation circuit 20 and the additional secondary flotation cell 300 can be combined for further processing.

Example 6

Detail B of yet another embodiment is shown in fig. 10. In this variant, the secondary flotation circuit 20 comprises three secondary flotation cells 210a, 210b, 210c arranged in series.

In this embodiment, the primary overflow 51a from the first rougher primary flotation cell 111a is directed into the first secondary flotation cell 210a, while the primary overflow 51b from the second rougher primary flotation cell 111b is directed into the first further secondary flotation cell 110 b. The secondary underflow 42a from the first secondary flotation cell 210a is directed into a first additional secondary flotation cell 210 b. The secondary underflow 42b from this flotation cell is further directed to a second additional secondary flotation cell 210c in fluid communication with the previous secondary flotation cell 210 b. From here, the secondary underflow 42c is still further directed to an additional secondary flotation cell 300. The secondary overflows 50a, 50b, 50c and 50 from the respective secondary flotation cells 210a, 210b, 210c and 300 are recovered as a first concentrate 81. The final secondary underflow 42' is drawn from the additional secondary flotation tank 300 as tailings 83.

The primary overflow 51c, 51d, 51e from the third, fourth and fifth rougher primary flotation cells 111c, 111d, 111e is first collected in a collection conduit 510 and directed as an inflow to the additional secondary flotation cell 300 for separation into an overflow 50 and an underflow 42', as shown in examples 5 and 6.

Example 7

In one embodiment of the invention, the detail B of which is shown in fig. 11, the rougher section 11 of the primary flotation circuit 10 also comprises five rougher primary flotation cells 111a, 111B, 111c, 111d, 111 e. The two first rougher first-stage flotation cells 111a, 111b have a larger volume than the last three rougher first-stage flotation cells 111c, 111d, 111 e. However, the flotation process in the rougher section 11 of the primary flotation circuit 10 is similar to the flotation process of the previous example.

The secondary flotation circuit 20 includes three secondary flotation cells 210a, 201b, 300, the operation of which is similar to that described above. The secondary flotation tank 210a, 210b has a smaller volume than the two first rougher primary flotation tanks 111a, 111 b.

The additional secondary flotation tank 300 is arranged to receive the combined overflow 51c, 51d, 51e from the three last rougher primary flotation tanks 111c, 111d, 111e through collecting conduits 510. Since the total volume of the three last stage flotation cells 111b, 111c, 111d is smaller in this embodiment, the volume of the additional secondary flotation cell 300 can also be smaller, as shown in fig. 11.

The secondary underflow 42' from the additional secondary flotation tank 300 is withdrawn from the flotation apparatus 1 as a tailings stream 83, which tailings stream 83 may be combined with the tailings stream 83 of the primary flotation circuit 10. For example, the combined tailings stream may be introduced into another flotation device 1 for recovering the second concentrate 82.

The secondary overflow 50, 50a, 50b comprises the recovered first concentrate 81 for further processing in a manner similar to the other examples and embodiments.

Example 8

In fig. 12, a detail B of a further embodiment of the flotation device 1 is shown. In this embodiment, the rougher section 11 of the primary circuit 10 includes six rougher primary flotation cells 111a, 111b, 111c, 111d, 111e, 111 f. The flotation process in the rougher section 11 is similar to that described in connection with the previous examples.

The overflow 51a from the first rougher first flotation cell 111a is directed into the first secondary flotation cell 210a via conduit 500 to separate into an overflow 50a and an underflow 42a in the secondary flotation cell 210 a. The volume of the secondary flotation tank 210a may be less than the volume of the first rougher primary flotation tank 111 a. The overflow 50a is led out of the first secondary flotation cell 20 as a first concentrate 81 for further processing in any suitable manner.

The secondary underflow 42a from the first secondary flotation cell 210a, which may include a quantity of mineral ore particles containing valuable minerals, is directed to another secondary flotation cell 210b for further processing to recover any remaining mineral ore particles containing valuable minerals, thereby enhancing the recovery of such minerals within the flotation apparatus 1.

The primary overflow 51b, 51c from the second and third rougher primary flotation cells 111b, 111c is first collected in a collecting conduit 510 and directed together as an inflow into the other secondary flotation cell 210b for separation into a secondary overflow 50b and a secondary underflow 42 b. The volume of the secondary flotation tank 210b may be less than the total volume of the two rougher primary flotation tanks 111b, 111c from which it receives the overflow 51b, 51 c.

The secondary overflow 50b of the secondary flotation cell 210b is collected as the first concentrate 81 and the secondary underflow 42b is arranged to flow into an additional secondary flotation cell 300 for further processing.

The additional secondary flotation tank 300 is arranged to receive the combined overflow 51d, 51e, 51f from the three last rougher primary flotation tanks 111d, 111e, 111f through collecting conduits 510.

The underflow 42' from the additional secondary flotation cell 300 is withdrawn from the flotation apparatus 1 as a tailings stream 83, which tailings stream 83 may be combined with the tailings stream 83 of the primary flotation circuit 10 (not shown in fig. 12). For example, the combined tailings stream 83 may be introduced into another flotation device 1 to recover the second concentrate 82.

The overflow 50 of the additional secondary flotation tank 300 comprises the recovered first concentrate 81 for further processing in a similar manner as in connection with the other examples and embodiments.

Example 9

In fig. 13, a detail B of another embodiment of the flotation device 1 is shown. In this embodiment there are two primary flotation circuits, both comprising rougher sections 11a, 11 b. The two rougher sections 11a, 11b include five rougher primary flotation cells 111a-e, 121a-e, respectively. The two primary flotation circuits are arranged to treat the slurry stream similarly to, for example, examples 3 and 4.

However, the primary overflows 51a, 53a from the first rougher primary flotation cells 111a, 121a of the two rougher sections 11a, 11b are arranged to flow into a single secondary flotation cell 210 a. The secondary overflow 50a from the secondary flotation cell 210a is recovered as the first concentrate 81.

The secondary underflow 42 is split into two separate streams (i.e., the secondary underflow 42 from the first secondary flotation cell 210a is split into two separate streams within the first secondary flotation cell 210a, or the underflow 42 may be split into two streams downstream of the first secondary flotation cell 210 a) and directed downstream into two additional secondary flotation cells: a first additional secondary flotation tank 300a for receiving the combined overflow 51b, 51c, 51d, 51e from the last four rougher primary flotation tanks 111b, 111c, 111d, 111e of the rougher section 10a of the first primary flotation circuit through collecting conduits 510; a second additional secondary flotation tank 300b arranged to receive the combined overflow 53b, 53c, 53d, 53e from the last four rougher primary flotation tanks 121b, 121c, 121d, 121e of the rougher section 10b of the second primary flotation circuit via collecting conduits 520.

Similarly to what is described in example 8, the underflow 42' from the additional secondary flotation cells 300a, 300b is led out of the flotation apparatus 1 as a tailings stream 83, which tailings stream 83 may be combined with the tailings stream 83 of the primary flotation circuit (not shown in the figure). The overflow 50b of the additional secondary flotation tank 300a, 300b comprises the recovered first concentrate 81 for further processing in a similar manner to the other examples and embodiments.

Example 10

In fig. 14, a detail B of another embodiment of the flotation device 1 is shown. It basically comprises the same constructional details as the arrangement of example 8 (see fig. 12), but instead of only the slurry being aerated in each single flotation cell 111, 210 and divided into two parts (overflow and underflow) in the single flotation cell, each flotation circuit 10, 20 comprises a first preliminary flotation cell 115, 215 and a flotation cell 111, 210 adjacent to the preliminary flotation cell 115, 215 by means of a hydraulic conduit 41. In the prefloating tanks 115, 215, the slurry stream is aerated by means of a stirrer provided with gas inlet means or by means of a bubbling aeration device. The adjacent flotation cells 111, 210 are operated in a flotation cell mode without mechanical agitation to ensure bubble-ore particle agglomeration stability and formation of an undisturbed froth layer. The scavenger section of the primary flotation circuit may also include a similar prefloat cell-flotation cell combination, but is not shown in fig. 14.

The slurry inflow 100 is first introduced into the rougher section 11 of the primary flotation circuit of the flotation plant. The slurry is more specifically introduced into the prefloat cell 115a for treatment in the manner previously described. From the prefloat cell 115a, the slurry stream is directed via a hydraulic conduit 41 to a rougher first stage flotation cell 111a, from which first stage flotation cell 111a the overflow 51a is directed via the hydraulic conduit 41 to a first secondary flotation circuit 20 comprising a similar prefloat cell 215a and an adjacent flotation cell 210 a.

The primary underflow 40 from the rougher primary flotation cell 111a of the primary flotation circuit 10 is directed downstream for similar treatment in the additional prefloat cells 115 and the rougher primary flotation cell 111 of the rougher section 11 until the primary underflow 40 of the last flotation cell 111f is directed to a scavenger section similar to the other embodiments of the present invention.

The secondary underflow 42a from the flotation cell 210a of the secondary flotation circuit 20 is directed downstream for similar treatment in another secondary preparation cell 215b and another flotation cell 210 b. The combined primary overflow 51b, 51c from the rougher primary flotation tank 111b, 111c (both also preceded by the pref iotaguration tank 115b, 115c) is directed via a collecting conduit 510 into the pref iotaguration tank 215b of the other secondary flotation tank 210 b. The underflow 42b from another secondary flotation tank 210b is directed downstream to the preliminary tank 315 of the additional secondary flotation tank 300.

The secondary overflow 50a from the first secondary flotation cell 210a and the secondary overflow 50b from the other secondary flotation cell 210b are directed out of the secondary flotation circuit 20 as the first concentrate 81.

The combined overflow 51d, 51e, 51f from the further rougher primary flotation tank 111d, 111e, 111f is led via a collecting duct 510 to the prefloat tank 315 of the additional secondary flotation tank 300. The overflow 50 from the additional secondary flotation cell 300 comprises the recovered first concentrate 81. The underflow 42' from the additional secondary flotation circuit 23 can be led out of the flotation device 1 as tailings stream 83.

Example 11

In fig. 15, an embodiment of a flotation system 9 according to the invention is shown.

The flotation system 9 comprises two flotation devices 1a, 1b of a type similar to that of example 4, but which may be of any of the types given in the examples above. The first flotation device 1a is used to recover a first concentrate 81 and the second flotation device 1b is used to recover a second concentrate 82.

The rougher primary flotation cells 111a-e of the rougher section 11a of the first flotation device 1a and the rougher primary flotation cells 121a-e of the rougher section 11b of the second flotation device 1b are arranged in series.

Since the function and arrangement of the flow paths of the flotation devices 1a, 1b have been discussed in detail in connection with the above examples, the details of the flotation devices 1a, 1b will not be discussed here.

The underflow 40' of the last scavenger primary flotation cell 112b of the scavenger section 12a of the primary flotation circuit 10a of the first flotation device 1a is directed to a device adapted for further treatment of the mineral ore particles suspended in the slurry. In one embodiment, the apparatus may be a grinding step 62, or in another embodiment, an apparatus 65 for adding flotation chemicals. (in FIG. 15, the apparatus is shown by way of example only, it being understood that depending on the embodiment, the block may represent a grinding step 62 or an apparatus 65 for adding flotation chemicals.)

In embodiments where the plant includes a grinding step 62, the second concentrate 82 recovered in the second flotation plant 1b contains ore particles that contain the same valuable minerals as the first concentrate 81 recovered in the first flotation plant 1a (i.e. both concentrates have the same or similar mineral composition), but the particle size distribution of the second concentrate 82 is different due to the grinding step 62.

Alternatively, the further processing step may comprise readjustment of the slurry flow collected as underflow 40' of the first flotation device 1a, i.e. treatment of the slurry with additional flotation chemicals, in order to prepare the slurry inflow 100b for recovery of the second concentrate 82. In this case, the second concentrate 82 recovered in the second flotation unit 1b contains ore particles containing different valuable minerals than the first concentrate 81 recovered in the first flotation unit 1 a. Thus, the two concentrates have different mineral compositions.

In one embodiment, the second concentrate 82 collected from the last two rougher primary flotation cells 111c-d of the rougher section 11b of the second primary flotation circuit 10b as the primary overflow 51c-d may be combined and directed to further processing, which may not be an additional secondary flotation cell 300 as in the first flotation circuit 10a, but may be any suitable further processing or operation known in the art, such as a further concentration flotation operation in a rougher concentration flotation circuit. The overflow 52a, 52b of the scavenger primary flotation cells 112a, 112b of both flotation apparatuses 1a, 1b can be treated as described earlier in this specification either by directing the overflow to the regrinding step 64 and to the scavenger concentration flotation circuit or by directing the overflow back to the primary flotation circuit (see figure 3).

The various embodiments described above may be used in any combination with each other. Several embodiments may be combined together to form another embodiment. The present disclosure may be directed to an apparatus, method, system or use comprising at least one of the embodiments described above. It is obvious to a person skilled in the art that with the advancement of technology, the basic idea of the invention may be implemented in various ways. The invention and its embodiments are thus not limited to the examples described above, but may vary within the scope of the claims.

Claims

1. A flotation apparatus for processing mineral ore particles suspended in a slurry, the flotation apparatus comprising a flotation cell for separating the slurry into an underflow and an overflow, wherein the separation is performed with the aid of a flotation gas, and wherein the flotation apparatus comprises a primary flotation circuit,

the primary flotation circuit comprises a rougher section having at least two rougher primary flotation cells connected in series and arranged in fluid communication, the overflow from the first rougher primary flotation cell being arranged to flow directly into the secondary flotation circuit,

the primary flotation circuit comprises a scavenger section having at least two scavenger primary flotation cells connected in series and arranged in fluid communication, the overflow from the scavenger primary flotation cells being arranged to flow back into the rougher primary flotation cells of the primary flotation circuit or to a regrinding step and then to a scavenger concentration flotation circuit,

wherein a subsequent stage flotation tank is arranged to receive a stage underflow from a preceding stage flotation tank;

the secondary flotation circuit comprises at least two secondary flotation cells, wherein in the secondary flotation circuit a first secondary flotation cell is arranged in fluid communication with at least one rougher primary flotation cell and is arranged to receive a primary overflow from the at least one rougher primary flotation cell for recovering a first concentrate,

it is characterized in that in a secondary flotation circuit,

a further secondary flotation cell is arranged in fluid communication with the at least one further rougher primary flotation cell and is arranged to receive a primary overflow from the at least one further rougher primary flotation cell for recovering the first concentrate,

the other secondary flotation cell is arranged in fluid communication with the preceding secondary flotation cell, and

the underflow from the first secondary flotation cell is arranged to flow into the further secondary flotation cell or is arranged to be combined with the secondary underflow of the further secondary flotation cell.

2. The flotation device of claim 1, wherein at least one of the secondary flotation cells of the secondary flotation circuit is arranged in direct fluid communication with a first rougher primary flotation cell from which it receives a primary overflow.

3. The flotation device of claim 1, wherein the secondary flotation cell is arranged to receive a primary overflow from at most two rougher primary flotation cells.

4. A flotation device according to claim 3, wherein the secondary flotation cell is arranged to receive a primary overflow from a rougher primary flotation cell.

5. The flotation device of claim 1, wherein the further secondary flotation cell is arranged to receive a primary overflow from at least two rougher primary flotation cells.

6. A flotation device according to any one of claims 1 to 5, wherein the underflow from the further secondary flotation cell is arranged to flow back to the rougher section of the primary flotation circuit at a point downstream of the rougher primary flotation cell from which the further secondary flotation cell receives the primary overflow.

7. A flotation device according to claim 6, wherein the underflow from the further secondary flotation cell is arranged to flow back to the further rougher primary flotation cell downstream of the first rougher primary flotation cell from which the further secondary flotation cell receives a primary overflow.

8. A flotation device according to claim 6, wherein the underflow from the further secondary flotation cell is arranged to be combined with the overflow from at least one further rougher primary flotation cell downstream of the rougher primary flotation cell from which the further secondary flotation cell receives the overflow.

9. The flotation device according to any one of claims 1 to 5, wherein the secondary flotation circuit further comprises an additional secondary flotation circuit comprising at least one additional secondary flotation cell arranged to receive a primary overflow from at least one other rougher primary flotation cell.

10. The flotation device of claim 9, wherein the underflow from the other secondary flotation cell is arranged to flow into an additional secondary flotation cell.

11. A flotation device according to claim 9, wherein the first secondary flotation cell is arranged to receive a primary overflow from a first rougher primary flotation cell and the additional secondary flotation cell is arranged to receive a primary overflow from at least two other rougher primary flotation cells.

12. The flotation apparatus of any one of claims 1 to 5, wherein underflow from another secondary flotation cell is arranged to flow into a last rougher primary flotation cell of the at least one rougher primary flotation cell from which the another secondary flotation cell receives a primary overflow, or into a rougher primary flotation cell downstream of the last rougher primary flotation cell of the at least one rougher primary flotation cell from which the another secondary flotation cell receives a primary overflow.

13. The flotation device according to any one of claims 1 to 5, wherein the volume of the first secondary flotation cell of the secondary flotation circuit is larger than the volume of the other secondary flotation cell of the secondary flotation circuit.

14. The flotation device according to any one of claims 1 to 5, wherein the volume of the further secondary flotation cell of the secondary flotation circuit is larger than the volume of the first secondary flotation cell of the secondary flotation circuit.

15. The flotation device according to any one of claims 1 to 5, wherein the volume of the first secondary flotation cell in fluid communication with at least one rougher primary flotation cell is 2-50% of the total volume of the at least one rougher primary flotation cell.

16. The flotation device according to any one of claims 1 to 5, wherein the volume of the further secondary flotation cell in fluid communication with at least one rougher primary flotation cell is 2-50% of the total volume of the at least one rougher primary flotation cell.

17. A flotation device according to any one of claims 1 to 5, wherein the primary overflow from at least one scavenger primary flotation cell is arranged to flow directly into the regrinding step.

18. A flotation device according to any one of claims 1 to 5, wherein the combined primary overflow from the scavenger primary flotation cell is arranged to flow directly into the regrinding step.

19. The flotation device according to any one of claims 1 to 5, wherein the combined secondary overflow of the at least two secondary flotation cells is arranged to flow into a further processing step.

20. A flotation device according to any one of claims 1 to 5, wherein the underflow from the last scavenger primary flotation cell is arranged to flow to further processing steps or to leave the flotation device as tailings.

21. A flotation device according to any one of claims 1 to 5, wherein the underflow from the last secondary flotation cell is arranged to flow to further processing steps or to leave the flotation device as tailings.

22. The flotation device according to any one of claims 1-5, wherein the flotation device comprises two primary flotation circuits, and the first secondary flotation cell of the secondary flotation circuit is arranged to receive overflow from the first rougher primary flotation cell of the two primary flotation circuits.

23. The flotation device according to any one of claims 1 to 5, wherein the flotation cell comprises a froth flotation cell.

24. The flotation device of claim 23, wherein the third rougher primary flotation cell and any subsequent rougher primary flotation cells after the third rougher primary flotation cell comprise froth flotation cells.

25. The flotation device of claim 23, wherein the first rougher primary flotation cell and the second rougher primary flotation cell operate as overflow flotation cells.

26. The flotation device of claim 23, wherein the flotation gas is fed to a flotation tank which separates the slurry into an overflow and an underflow.

27. The flotation device of claim 23, wherein the flotation cell into which the flotation gas is fed includes a mixer.

28. A flotation device according to claim 23, characterized in that the flotation gas is fed into a prefloating cell in which a mixer is arranged.

29. A flotation device according to any one of claims 1 to 5, wherein the mineral ore particles comprise Cu, or Zn, or Fe, or pyrite, or metal sulfides.

30. A flotation system, characterized in that it comprises a flotation device according to any one of claims 1-29.

31. The flotation system according to claim 30, wherein the flotation system comprises at least two or at least three flotation devices according to any one of claims 1-29.

32. The flotation system according to claim 30, wherein the flotation system comprises at least one first flotation device for recovering a first concentrate and at least one second flotation device for recovering a second concentrate.

33. The flotation system according to claim 32, wherein the primary flotation cell of the at least one first flotation device for recovering a first concentrate and the primary flotation cell of the at least one second flotation device for recovering a second concentrate are arranged in series.

34. The flotation system according to claim 32 or 33, wherein the flotation system comprises means for further processing the mineral ore particles suspended in the slurry such that the second concentrate is different from the first concentrate.

35. The flotation system of claim 34, wherein the means for further processing the mineral ore particles suspended in the slurry includes a grinding step disposed between the first flotation device and the second flotation device.

36. The flotation system of claim 34, wherein the means for further processing the ore particles suspended in the slurry includes means for adding flotation chemicals disposed between the first flotation device and the second flotation device.

37. The flotation system according to claim 30, wherein the flotation device is arranged to recover mineral ore particles containing Cu and/or Zn and/or pyrite and/or to recover metals from sulphides.

38. The flotation system according to claim 30, wherein the flotation device is arranged to recover mineral ore particles containing Cu from low grade ore.

39. The flotation system according to claim 30, wherein the flotation device is arranged to recover Fe by reverse flotation.